Titanium tower internals can absorb hydrogen and form brittle hydrides under reducing, hydrogen-generating, or excessively cathodic conditions. Galvanic coupling may increase risk even while visible corrosion remains low. Reliable prevention requires full chemistry review, control of dissimilar-metal contacts, suitable grade and product form, low-stress geometry, exceptionally clean and well-shielded welding, and inspection methods beyond wall-thickness measurement.

Unintended siphoning can continue draining tower distributors, collectors, wash lines, and internal transfer pipes after pumps stop. It requires a continuous liquid column, favorable elevation difference, and no effective gas entry at the high point. Prevention combines transient elevation and pressure analysis, correctly located and sized siphon breaks, safe vent destinations, blockage-resistant geometry, and pump-trip testing. Check valves alone may not provide dependable protection.

Liquid trapped inside sealed or poorly vented hollow tower internals can generate damaging pressure through thermal expansion, vaporization, freezing, chemical reaction, or delayed equalization during depressurization. Prevention requires a cavity register, an intentional sealed-or-vented philosophy, qualified closure welds, correctly located vents and drains, dryness verification, and cautious inspection before hot work or drilling. Unknown holes should never be plugged without understanding their pressure-relief or telltale function.

Environmental stress cracking occurs when a susceptible thermoplastic, damaging chemical, and tensile stress combine, often below short-term yield strength. Reliable tower-internal design requires exact resin-grade selection, service-specific long-term testing, low-stress geometry, thermal-movement allowance, controlled welding and tightening, and inspection of notches, holes, welds, and restrained connections. It is a distinct mechanism from ordinary corrosion, swelling, or thermal creep.

Ship and offshore motion repeatedly tilts liquid surfaces, redistributes tray and packed-bed flow, changes downcomer seals, creates sloshing loads, and applies cyclic forces to tower internals. Reliable FPSO and FLNG design requires a defined six-degree-of-freedom motion basis, orientation-sensitive hydraulic analysis, adequate distributor head and freeboard, controlled compartmentation, packing restraint, and fatigue-resistant supports. Stationary performance tests alone cannot demonstrate suitability at sea.