Jieun Yang
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6 records found
1
Gas Fraction in an Alkaline Water Electrolysis Cell
Wall-resolved measurements with X-ray imaging
This thesis measures the steady-state gas fraction in a classical alkaline water electrolyser using X-ray imaging. The cell was purpose-built for the experiment: a wide inter-electrode gap of 114 mm filled with 6 M KOH, with no forced flow, so that the near-wall layer develops unconfined. Time-averaged radiographs are converted through the Beer–Lambert law into a two-dimensional gas-fraction field ε(x, y), at a pixel size of 45 μm, for current densities j spanning from 36.5 A m−2 to 2434 A m−2, and for both the hydrogen and the oxygen electrode.
The measured fields show a thin near-wall layer that decays into an almost gas-free bulk. The peak gas fraction is set by the current density, growing roughly as √j to about 0.2 at the highest current, while the width of the layer is set dominantly by height, broadening steadily at the highest current from about 0.3 mm at the bottom to 1.5 mm at the top of the 87 mm of electrode height captured in the field of view, and changing only weakly with current. It is therefore the current that fixes how much gas the layer holds at its peak, and the vertical length of the electrode that fixes how far that gas spreads horizontally. At equal current density the hydrogen side carries about twice the near-wall gas fraction of the oxygen side, in line with the reaction stoichiometry; matched for gas production, the hydrogen peak is the higher and the oxygen layer the wider, so the two sides hold much the same near-wall gas but arrange it differently. Only the hydrogen side develops a dispersed-gas background, which builds up towards the top of the cell to a gas fraction of about 0.026 at the highest current, whereas the oxygen side stays close to the detection floor.
Interpreted via a one-dimensional production–removal balance, the profiles imply an apparent lateral dispersion coefficient of order 10−7 m2 s−1. It is not a material constant: it grows with both current and height and varies by over an order of magnitude, and is best read as an apparent, lumped quantity. A likely, but unproven, reading is that a crowding of gas bubbles, a solid pressure, caps the near-wall peak while dispersion sets the width of the layer.
The experimental data from this study thus provide an unconfined, wall-resolved reference for the gas fraction in an alkaline electrolyser, useful for reasoning about the physics of the near-wall layer, for validating transport models and for cell design, though transfer to pressurised, forced-flow or zero-gap cells needs further validation. ...
This thesis measures the steady-state gas fraction in a classical alkaline water electrolyser using X-ray imaging. The cell was purpose-built for the experiment: a wide inter-electrode gap of 114 mm filled with 6 M KOH, with no forced flow, so that the near-wall layer develops unconfined. Time-averaged radiographs are converted through the Beer–Lambert law into a two-dimensional gas-fraction field ε(x, y), at a pixel size of 45 μm, for current densities j spanning from 36.5 A m−2 to 2434 A m−2, and for both the hydrogen and the oxygen electrode.
The measured fields show a thin near-wall layer that decays into an almost gas-free bulk. The peak gas fraction is set by the current density, growing roughly as √j to about 0.2 at the highest current, while the width of the layer is set dominantly by height, broadening steadily at the highest current from about 0.3 mm at the bottom to 1.5 mm at the top of the 87 mm of electrode height captured in the field of view, and changing only weakly with current. It is therefore the current that fixes how much gas the layer holds at its peak, and the vertical length of the electrode that fixes how far that gas spreads horizontally. At equal current density the hydrogen side carries about twice the near-wall gas fraction of the oxygen side, in line with the reaction stoichiometry; matched for gas production, the hydrogen peak is the higher and the oxygen layer the wider, so the two sides hold much the same near-wall gas but arrange it differently. Only the hydrogen side develops a dispersed-gas background, which builds up towards the top of the cell to a gas fraction of about 0.026 at the highest current, whereas the oxygen side stays close to the detection floor.
Interpreted via a one-dimensional production–removal balance, the profiles imply an apparent lateral dispersion coefficient of order 10−7 m2 s−1. It is not a material constant: it grows with both current and height and varies by over an order of magnitude, and is best read as an apparent, lumped quantity. A likely, but unproven, reading is that a crowding of gas bubbles, a solid pressure, caps the near-wall peak while dispersion sets the width of the layer.
The experimental data from this study thus provide an unconfined, wall-resolved reference for the gas fraction in an alkaline electrolyser, useful for reasoning about the physics of the near-wall layer, for validating transport models and for cell design, though transfer to pressurised, forced-flow or zero-gap cells needs further validation.
Offshore decommissioning is accelerating asageing oil and gas infrastructure reaches the end of its service life. In theNorth Sea alone, over 2,650 wells are scheduled between 2025 and 2034, and wellplug and abandonment accounted for 49% of decommissioning expenditure on the UKContinental Shelf in 2024. Within this scope, conductor removal, the extractionof large-diameter vertical steel pipes connecting subsea wells to surfacefacilities, remains a persistent operational bottleneck. Current practice relieson the cut-and-pull method, in which the entire lifting load is transferredthrough a single conductor cross-section. Its applicability is thereforegoverned by the structural condition of that cross-section, as corroded casingsand degraded connections may not sustain the concentrated load.
This thesis proposes a compliant grippingmechanism that distributes the lifting load over the outer conductor surface,and examines whether it scales to the multi-tonne loads of conductor removal, aregime far beyond the small-scale applications to which soft robotic grippershave been confined. Following a literature study into soft gripping methods anda conceptual design process, four concepts were evaluated, from which a braidedconstriction sleeve gripper was selected. Its defining property is aself-forcing mechanism, in which the weight of the conductor tightens the braidaround its surface, so that a heavier load produces a stronger grip.
An analytical model relates the braidgeometry to the holding capacity, which grows exponentially with adimensionless self-forcing coefficient. This coefficient is the product of thefriction coefficient and a geometric coefficient scaling with the conductorradius and the square of the number of braid turns, and inversely with thegripping length. The capacity is supplied passively by the weight of a bottomring, requiring no continuous actuation. A parametric campaign across twelveconfigurations, each tested five times, supported the model within the rangeexamined. The measured capacity scaled linearly with the ring weight at fixedgeometry, rose far more steeply with the geometric coefficient than preloadfriction alone permits, following the exponential form characteristic ofself-forcing, and followed the predicted direction for each geometric parametervaried in isolation. A single friction coefficient of approximately 0.135reproduced the measured capacity across differing geometries, supporting thecontact assumptions. The most tightly braided configuration sustained more than75 kg without slipping, giving a payload-to-self-weight ratio of at least 337:1against 16:1 at the baseline.Applied to the NorthCormorant platform, the model yields an early-phase full-scale design employinga steel wire rope braid of seven turns over a gripping length of 14 metres,preloaded by a 10 tonne bottom ring. Under a conservative design frictioncoefficient of 0.10, the holding capacity reaches approximately 18,800 kNagainst a design lifting weight of 634 kN per conductor section. Slip istherefore not the governing constraint, which is set instead by the ropestrength at the top ring connection and by the deployment of the braid. To theauthor's knowledge, this constitutes the first compliant gripping conceptmodelled, experimentally supported, and dimensioned for offshore removals atthe multi-tonne scale. ...
Offshore decommissioning is accelerating asageing oil and gas infrastructure reaches the end of its service life. In theNorth Sea alone, over 2,650 wells are scheduled between 2025 and 2034, and wellplug and abandonment accounted for 49% of decommissioning expenditure on the UKContinental Shelf in 2024. Within this scope, conductor removal, the extractionof large-diameter vertical steel pipes connecting subsea wells to surfacefacilities, remains a persistent operational bottleneck. Current practice relieson the cut-and-pull method, in which the entire lifting load is transferredthrough a single conductor cross-section. Its applicability is thereforegoverned by the structural condition of that cross-section, as corroded casingsand degraded connections may not sustain the concentrated load.
This thesis proposes a compliant grippingmechanism that distributes the lifting load over the outer conductor surface,and examines whether it scales to the multi-tonne loads of conductor removal, aregime far beyond the small-scale applications to which soft robotic grippershave been confined. Following a literature study into soft gripping methods anda conceptual design process, four concepts were evaluated, from which a braidedconstriction sleeve gripper was selected. Its defining property is aself-forcing mechanism, in which the weight of the conductor tightens the braidaround its surface, so that a heavier load produces a stronger grip.
An analytical model relates the braidgeometry to the holding capacity, which grows exponentially with adimensionless self-forcing coefficient. This coefficient is the product of thefriction coefficient and a geometric coefficient scaling with the conductorradius and the square of the number of braid turns, and inversely with thegripping length. The capacity is supplied passively by the weight of a bottomring, requiring no continuous actuation. A parametric campaign across twelveconfigurations, each tested five times, supported the model within the rangeexamined. The measured capacity scaled linearly with the ring weight at fixedgeometry, rose far more steeply with the geometric coefficient than preloadfriction alone permits, following the exponential form characteristic ofself-forcing, and followed the predicted direction for each geometric parametervaried in isolation. A single friction coefficient of approximately 0.135reproduced the measured capacity across differing geometries, supporting thecontact assumptions. The most tightly braided configuration sustained more than75 kg without slipping, giving a payload-to-self-weight ratio of at least 337:1against 16:1 at the baseline.
Applied to the NorthCormorant platform, the model yields an early-phase full-scale design employinga steel wire rope braid of seven turns over a gripping length of 14 metres,preloaded by a 10 tonne bottom ring. Under a conservative design frictioncoefficient of 0.10, the holding capacity reaches approximately 18,800 kNagainst a design lifting weight of 634 kN per conductor section. Slip istherefore not the governing constraint, which is set instead by the ropestrength at the top ring connection and by the deployment of the braid. To theauthor's knowledge, this constitutes the first compliant gripping conceptmodelled, experimentally supported, and dimensioned for offshore removals atthe multi-tonne scale.Multi-Directional Vibrational Energy Harvester with In-Plane Motion
Exploiting Degenerate Modes
Towards prestressing neutrally stable joints with pressure
Experimentation and parameter study on a spatial compliant enclosed volume joint