A New Impinging Jet Device for Corrosion Studies

ABSTRACTA new high-pressure, high-temperature submerged impinging jet device is described. The experimental results of its flow characteristics are summarized. The device generates welldeveloped steady flow in the jet tubes with laminar flow up to Reynolds numbers (Re) of 1,980 and turbulent flow ab...

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Published inCorrosion (Houston, Tex.) Vol. 60; no. 5; pp. 455 - 464
Main Authors Demoz, A., Dabros, T., Michaelian, K., Papavinasam, S., Revie, W.
Format Journal Article
LanguageEnglish
Published Houston, TX NACE International 01.05.2004
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Abstract ABSTRACTA new high-pressure, high-temperature submerged impinging jet device is described. The experimental results of its flow characteristics are summarized. The device generates welldeveloped steady flow in the jet tubes with laminar flow up to Reynolds numbers (Re) of 1,980 and turbulent flow above Re = 2,800. Local mass transfers were measured on a polytetrafluoroethylene (PTFE) disc normal to the jet using eight 1-mm-diameter microelectrodes located at 0 < x/r < 3.8, where x is the distance from the stagnation point on the disc and r is the jet nozzle radius. Measurements were made using the limiting current of potassium ferricyanide (K3Fe[CN]6) solution electrochemical reduction for 50 Re 4,500 at H/r = 10, where H is the height of the jet nozzle exit above the PTFE disc. Flow transition from laminar to turbulent flow at the flat disc occurred at Re 800. The dependence of the local Sherwood number (Sh) on x/r gave three flow regions: x/r < 1; 1 x/r 2; and x/r > 2. This correlation further indicated that the flow from x/r = 2 and beyond was in the wall jet region. The empirical relation between Sh and Re in the stagnation region and developing wall jet region gave two segmented linear correlations. The device is scalable and can generate a wide range of Re. The empirical wall shear stress of the impinging jet was found to be more than 90 times that calculated for the rotating cylinder electrode (RCE) at comparable size and Re. This new device, therefore, is well suited for inhibitor and corrosion studies at high wall shear stress.
AbstractList ABSTRACTA new high-pressure, high-temperature submerged impinging jet device is described. The experimental results of its flow characteristics are summarized. The device generates welldeveloped steady flow in the jet tubes with laminar flow up to Reynolds numbers (Re) of 1,980 and turbulent flow above Re = 2,800. Local mass transfers were measured on a polytetrafluoroethylene (PTFE) disc normal to the jet using eight 1-mm-diameter microelectrodes located at 0 < x/r < 3.8, where x is the distance from the stagnation point on the disc and r is the jet nozzle radius. Measurements were made using the limiting current of potassium ferricyanide (K3Fe[CN]6) solution electrochemical reduction for 50 Re 4,500 at H/r = 10, where H is the height of the jet nozzle exit above the PTFE disc. Flow transition from laminar to turbulent flow at the flat disc occurred at Re 800. The dependence of the local Sherwood number (Sh) on x/r gave three flow regions: x/r < 1; 1 x/r 2; and x/r > 2. This correlation further indicated that the flow from x/r = 2 and beyond was in the wall jet region. The empirical relation between Sh and Re in the stagnation region and developing wall jet region gave two segmented linear correlations. The device is scalable and can generate a wide range of Re. The empirical wall shear stress of the impinging jet was found to be more than 90 times that calculated for the rotating cylinder electrode (RCE) at comparable size and Re. This new device, therefore, is well suited for inhibitor and corrosion studies at high wall shear stress.
A new high-pressure, high-temperature submerged impinging jet device is described. The experimental results of its flow characteristics are summarized. The device generates well developed steady flow in the jet tubes with laminar flow up to Reynolds numbers (Re) of 1,980 and turbulent flow above Re = 2,800. Local mass transfers were measured on a polytetrafluoroethylene (PTFE) disc normal to the jet using eight 1-mm-diameter microelectrodes located at 0 < x /r < 3.8, where x is the distance from the stagnation point on the disc and r is the jet nozzle radius. Measurements were made using the limiting current of potassium ferricyanide (K3Fe[CN]6) solution electrochemical reduction for 50 # < Re # < 4,500 at H/r = 10, where H is the height of the jet nozzle exit above the PTFE disc. Flow transition from laminar to turbulent flow at the flat disc occurred at Re = 800. The dependence of the local Sherwood number (Sh) on x/r gave three flow regions: x/r < 1; 1 # < x/r # < 2; and x/r > 2. This correlation further indicated that the flow from x/r = 2 and beyond was in the wall jet region. The empirical relation between Sh and Re in the stagnation region and developing wall jet region gave two segmented linear correlations. The device is scalable and can generate a wide range of Re. The empirical wall shear stress of the impinging jet was found to be more than 90 times that calculated for the rotating cylinder electrode (RCE) at comparable size and Re. This new device, therefore, is well suited for inhibitor and corrosion studies at high wall shear stress.
A new high-pressure, high-temperature submerged impinging jet device is described. The experimental results of its flow characteristics are summarized. The device generates well-developed steady flow in the jet tubes with laminar flow up to Reynolds numbers (Re) of 1,980 and turbulent flow above Re = 2,800. Local mass transfers were measured on a polytetrafluoroethylene (PTFE) disc normal to the jet using eight 1-mm-diameter microelectrodes located at 0 < x/r < 3.8, where x is the distance from the stagnation point on the disc and r is the jet nozzle radius. Measurements were made using the limiting current of potassium ferricyanide (K3Fe[CN]6) solution electrochemical reduction for 50 ≤ Re ≤ 4,500 at H/r = 10, where H is the height of the jet nozzle exit above the PTFE disc. Flow transition from laminar to turbulent flow at the flat disc occurred at Re ≈ 800. The dependence of the local Sherwood number (Sh) on x/r gave three flow regions: x/r < 1; 1 ≤ x/r ≤ 2; and x/r > 2. This correlation further indicated that the flow from x/r = 2 and beyond was in the wall jet region. The empirical relation between Sh and Re in the stagnation region and developing wall jet region gave two segmented linear correlations. The device is scalable and can generate a wide range of Re. The empirical wall shear stress of the impinging jet was found to be more than 90 times that calculated for the rotating cylinder electrode (RCE) at comparable size and Re. This new device, therefore, is well suited for inhibitor and corrosion studies at high wall shear stress.
Author Revie, W.
Papavinasam, S.
Demoz, A.
Dabros, T.
Michaelian, K.
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Issue 5
Keywords Turbulent flow
Corrosion
turbulent flow. wall shear stress
stagnation region
Shear stress
Sherwood number
limiting current
impinging jet
Mass transfer
Language English
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Snippet ABSTRACTA new high-pressure, high-temperature submerged impinging jet device is described. The experimental results of its flow characteristics are summarized....
A new high-pressure, high-temperature submerged impinging jet device is described. The experimental results of its flow characteristics are summarized. The...
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SubjectTerms Applied sciences
Chemical reduction
Corrosion
Corrosion environments
Corrosion inhibitors
Corrosion mechanisms
Cylinders
Diameters
Electrochemistry
Exact sciences and technology
Flow characteristics
Fluid dynamics
Fluid flow
High temperature
Jet nozzles
Laminar flow
Metals. Metallurgy
Microelectrodes
Polytetrafluoroethylene
Potassium
Potassium ferricyanide
Reynolds number
Rotating cylinders
Shear stress
Stagnation point
Steady flow
Tubes
Turbulent flow
Wall jets
Wall shear stresses
Title A New Impinging Jet Device for Corrosion Studies
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