Distinguish chemical attack, thermal shock and mechanical breakage by combining fracture appearance, bed location, process history, pressure-drop trends and comparison with unused samples. Replacement without root-cause analysis risks repeating the failure.

Conventional ceramic packing is suitable for many chemical towers, but high-purity applications may require limits on iron, alkali oxides or other trace constituents. Acid resistance and chemical purity should be specified separately.

Mixed-chemical service should be evaluated from the complete process composition, including impurities, reaction products, cleaning chemicals and upset conditions. Do not select ceramic packing using only the dominant chemical name.

Do not select ceramic tower packing from acid concentration alone. Always evaluate the specific acid, concentration range, operating temperature, impurities and process changes together before confirming material compatibility.

Ceramic packing surface area, void fraction and packing factor cannot by themselves determine tower pressure drop. Actual ΔP depends on gas velocity, liquid loading, fluid properties, bed height and bed condition. Catalogue values are inputs to hydraulic analysis, not substitutes for operating data.