| Active ingredient | Potassium permanganate (KMnO4) impregnated onto porous activated alumina. Loading is grade-specific and should be stated as a weight percentage with its measurement basis. | Oxidative treatment of selected contaminants in air and gas streams, including hydrogen sulfide and certain odor-causing compounds. | Request the declared KMnO4 loading, test method, batch certificate, and guidance on whether the loading is reported on an as-supplied or dry basis. |
| Alumina carrier | Porous activated alumina beads or pellets; carrier properties and impregnation method differ among grades. | Fixed-bed gas-phase treatment where a porous, solid oxidizing medium is required. | Confirm the carrier type, mechanical strength, moisture condition, and compatibility with the intended operating temperature and humidity. |
| Particle size | Common granular formats include approximately 3–5 mm; other sizes may be available for different bed designs. | Ventilation, odor-control, and process-gas filter beds. | Check the full particle-size distribution, undersize and oversize limits, and compatibility with the vessel, screen, and target pressure drop. |
| Bulk density | Grade-dependent; obtain the supplier’s measured value and test method rather than relying on a generic figure. | Used to estimate media mass, vessel loading, and shipping volume. | Request bulk density in a stated unit and confirm whether the result is loose-filled or tapped. |
| Hydrogen sulfide treatment | Oxidizing media can react with hydrogen sulfide; usable capacity depends on the grade and operating conditions. | Odor control and treatment of selected low-concentration gas streams. | Ask for capacity data under conditions representative of the inlet concentration, humidity, temperature, and required outlet limit. Do not assume a universal service life. |
| Other target contaminants | Some grades are used for selected sulfur compounds, formaldehyde, and other oxidizable contaminants; performance is contaminant- and condition-specific. | Industrial odor control and certain indoor or process-air purification systems. | Obtain contaminant-specific breakthrough or performance data. Confirm that the media is suitable for the complete gas mixture, not just one target compound. |
| Operating conditions | Allowable temperature, relative humidity, gas velocity, and contaminant concentration depend on the product grade and system design. | Fixed-bed systems in ventilation, process, and odor-control applications. | Request an operating envelope and design recommendations. Excess moisture, competing contaminants, or unsuitable conditions can affect performance. |
| Pressure drop and bed design | Pressure drop depends on particle size, bed depth, gas velocity, packing, and dust or fines content. | Retrofit or new fixed-bed filter installations. | Ask for pressure-drop information at the intended flow rate and confirm recommended bed depth, face velocity, and media change-out criteria. |
| Packaging and export logistics | Packaging options may include sealed bags or drums, subject to the supplier’s product and export arrangements. | International shipment, warehouse storage, and planned media replacement. | Confirm net weight, packaging material, pallet configuration, storage conditions, shelf-life guidance, and applicable transport documentation for the destination. |
| Quality and documentation | Documentation availability varies by supplier and destination market. | Procurement qualification, site acceptance, and traceability. | Request a current technical data sheet, safety data sheet, batch certificate, country of origin, and any required declarations or compliance documents. |
| Spent-media management | Spent media may contain reaction products and residual oxidant; classification depends on its composition and local regulations. | Planned maintenance and replacement of fixed-bed media. | Confirm handling, storage, disposal, and waste-classification requirements with qualified local professionals and relevant authorities. |