Home News Knowledges Reading KHC-F1001 by Its Numbers: Surface Area, Ozone Split and Strength

Reading KHC-F1001 by Its Numbers: Surface Area, Ozone Split and Strength

2026-10-29 2 readings

A catalyst datasheet is not a scorecard. Each figure on it is a constraint that propagates through the flowsheet, and two catalysts with the same headline removal rate can demand completely different reactors. Taking the SINOKLE KHC-F1001 carbon-based ozone catalyst apart item by item is a useful exercise for exactly that reason.

Specific surface area: the count of active sites

Surface area sets how many reaction sites a cubic metre of bed can offer. KHC-F1001 uses a high-grade activated carbon carrier with an iodine number above 1,100 mg/g and a specific surface area of 1,400 m²/g, well beyond the level of conventional carbon-based catalysts. The consequence is not only more contact between ozone and organics. The developed pore structure also adsorbs and traps trace organic pollutants, so the material runs an adsorption-plus-catalysis mechanism at the same time, and oxidation performance sits clearly above an ordinary catalyst of the same class.

Decomposition rate is the efficiency figure that matters

Decomposition rate describes how much of the dosed ozone the catalyst converts into reactive species rather than letting it leave in the off-gas. At a 90% ozone decomposition rate the ozone dosage falls significantly and the energy consumption of the generator falls with it. Pair that with an improvement in organic degradation capacity of more than 10 times and the old trade-off - more ozone for more chemical oxygen demand removal - stops being a law of nature.

There is a second-order effect worth counting. When decomposition sits at 90%, the residual ozone leaving the reactor is small enough that the off-gas destruct unit can be sized modestly, which shifts the balance of plant cost as well as the reagent cost. A catalyst that quotes a strong removal rate but a mediocre decomposition figure pushes that residual up, and the extra destruct capacity rarely appears in the side-by-side comparison. Multiply the difference across a five-year service life and the reagent saving is no longer the largest item.

Removal figures you can hold a supplier to

A chemical oxygen demand (COD) removal rate of 70% and a colour removal rate of 95% are the stable indicators for advanced oxidation of refractory wastewater. The mechanism behind them is straightforward: the catalyst accelerates ozone decomposition, hydroxyl radicals appear quickly, and large refractory molecules are mineralised to carbon dioxide and water. Chemical oxygen demand, colour and toxic organics come down together, biodegradability improves, and the biological stage downstream receives a lighter load.

Strength, pH window and service life

Mechanical strength of 95% means abrasion and erosion resistance and a very low breakage rate under long-term fluidisation and backwashing - the failure mode that quietly destroys bed performance in plants where the catalyst is assumed to be permanent. The pH operating range is 3-11, with resistance to acid, alkali and high temperature for stable operation across a wide spread of chemical environments. Service life runs 3-5 years, above the 2-3 years common in the industry, and simple regeneration restores activity after deactivation, which cuts packing replacement frequency and cost together.

Integration with CDFU and CDOF packages

KHC-F1001 is used in advanced wastewater treatment, municipal water treatment and circulating water treatment, covering oil-bearing wastewater from petroleum refining, landfill leachate, pharmaceutical wastewater, dyeing wastewater and coal chemical wastewater. In refining it can be paired with purely physical desalter de-oiling to form a complete front-end coalescing flotation de-oiling plus back-end carbon-based ozone advanced oxidation flowsheet. It can equally be matched with CDFU cyclonic dissolved gas flotation and CDOF ozone oxidation equipment packages, which brings the whole train down to a skid-mounted integrated unit with shorter residence time and a smaller footprint.

Physical form and what it means for loading

The iodine number is the figure worth asking about first, because it is measured on the raw carrier and it does not improve during service. A carbon advertised at 1,400 m²/g with a weak iodine number is telling you that the surface exists on paper and not in the pore structure that ozone can reach.

The product ships as black granules or extruded cylinders with a customisable sizing of 3-5 mm, a bulk density of 0.45-0.55 g/cm³ and a moisture content of 5%. Those three numbers decide the loading procedure, the backwash velocity and the pressure drop across a fresh bed, and they are the ones most often ignored when a catalyst is bought on surface area alone.

Put the parameters together and the engineering profile is legible: a high-surface-area carbon carrier, high catalytic activity at the core, super-hydrophilic modification to secure mass transfer, high stability for long cycles, easy regeneration to lower whole-life cost, and green chemistry to answer compliance questions. Six dimensions reinforcing one another. None of them is decisive alone - a high surface area without strength, service life and hydrophilicity behind it stays a laboratory advantage. From carrier selection through active-component loading to surface modification, every step in KHC-F1001 exists to deliver the same stable trio of 90% ozone decomposition, 70% chemical oxygen demand removal and 95% colour removal once the material is in a real plant.