Sterling Analytical provides platinum reforming catalyst testing, quantifying platinum, rhenium, and the contaminant and modifier elements that govern performance on naphtha reforming catalysts. Our ICP-OES testing supports refinery process engineers and catalyst technologists managing platforming or CCR (continuous catalyst regeneration) units, where catalyst condition directly drives octane yield, hydrogen production, and run length between regenerations.
Testing this catalyst is less about confirming a single number and more about confirming that the whole system — metal loading, metal ratio, chloride balance, and where the sample sits in its regeneration cycle — is still where it needs to be.
Reforming catalyst is a chlorided alumina support carrying platinum, rhenium, and any secondary metal (tin or iridium, depending on catalyst generation) at relatively low weight percent levels, alongside controlled trace modifiers. Accurate digestion has to fully recover the platinum group metals from the alumina matrix without losing volatile species or introducing contamination from the chloride-rich support itself.
Sterling Analytical applies digestion strategies suited to this matrix:
For spent or carbon-fouled catalyst pulled from a unit, oxidative pretreatment may be applied to remove coke deposits that can otherwise interfere with metal recovery.
Pt:Re (or Pt:Sn, Pt:Ir) ratio is reported alongside individual metal content, since the ratio — not just total metal loading — is often what the catalyst was specifically engineered around. Additional contaminant or modifier elements (silicon, calcium, magnesium) can be added depending on catalyst formulation and process concern.
A reforming catalyst reading correct total platinum content can still be functionally off-spec if the metal ratio or chloride level has drifted.
Metal ratio: Pt:Re and other bimetallic ratios are engineered deliberately, not incidentally — a shift in that ratio, even with total metal loading unchanged, can alter selectivity and stability in ways a single-element platinum result won’t reveal. Rhenium’s main role alongside platinum is improving stability against coking and deactivation; a catalyst that’s lost rhenium relative to platinum may show normal initial activity but shorter run length before the next regeneration is needed.
Chloride balance: Chloride content governs the acid function of the catalyst. Catalyst running chloride-low tends to lose isomerization and cracking activity, showing up as lower octane gain for a given severity; chloride-high catalyst can over-crack feed, reduce liquid yield, and accelerate certain deactivation pathways. Chloride balance shifts gradually with water and chloride injection rates in the unit, which is why it’s tracked as a routine operating parameter, not just checked reactively after a yield problem shows up.
Contaminant sensitivity: Reforming catalyst, particularly platinum-rhenium systems, can be notably sensitive to feed sulfur — even low part-per-million sulfur levels in feed can measurably affect catalyst performance and selectivity, which is why sulfur is tracked alongside the primary metals panel rather than treated as a minor afterthought. Sodium and other alkali contamination, often carried in from upstream desalting or hydrotreating, can also neutralize acid sites in a way that mimics chloride-low behavior even when chloride itself tests within range — another reason a full contaminant panel gives a more reliable diagnosis than testing platinum alone.
During platinum reforming catalyst testing, we frequently help identify:
These patterns are most useful when tracked over time against fresh catalyst baseline data, rather than evaluated from a single sample in isolation.
In a CCR unit, catalyst regeneration follows a defined sequence: coke is burned off in air, the catalyst is oxychlorinated to redisperse platinum that has agglomerated under reaction heat back into small, evenly distributed particles, and the catalyst is then dried and reduced with hydrogen before returning to the reactors. Each step is necessary, and each step temporarily changes the catalyst’s chloride and oxidation state.
This matters for testing in a specific way: a sample pulled from the regeneration section partway through this sequence will show a different chloride level and metal oxidation state than a sample pulled from the reactor circuit, and that difference reflects normal process operation rather than a catalyst problem. Without knowing where in the cycle a sample was taken, a chloride result that looks “off” against a single fixed target can be misread. This is why we ask for sample source and cycle position rather than evaluating every sample against one static specification.
Tin-promoted catalysts add a further wrinkle: tin’s primary role is limiting platinum agglomeration during the high-temperature regeneration step, rather than directly driving reforming chemistry the way rhenium does. A Pt-Sn catalyst and a Pt-Re catalyst pulled from the same point in a regeneration cycle can show meaningfully different expected metal and chloride profiles, which is part of why catalyst generation and metal system are worth confirming at the time of sample submission.
Required sample size: 5–10 grams of representative catalyst (typically pelletized or extrudate form).
Packaging guidelines:
If you’re testing a used or partially deactivated catalyst rather than fresh material, let us know — used catalyst can carry additional organic residue that affects digestion approach.
Standard turnaround: 3–5 business days Rush service: 24–48 hours available
Pricing starts from $150 per sample, depending on element panel and whether chloride determination is included. Volume pricing available for routine monitoring programs.
Your COA includes:
All results are supported by CRM-traceable calibration, with duplicates and matrix spikes performed on each analytical batch.
Sterling Analytical applies established methods adapted for platinum-rhenium and related reforming catalyst materials:
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