An acidophilic bioleaching system for recovery of platinum group metals (PGMs) from spent automotive catalysts and hydroprocessing catalysts. Acidithiobacillus thiooxidans is the only organism the cited sources name: it generates sulfuric acid that dissolves the alumina support. The thiosulfate used for PGM complexation was sourced separately, from a biogas biodesulfurization bioreactor whose community the source does not characterise taxonomically. Spent three-way catalysts (TWC) from automotive exhaust systems contain precious metals (Pt, Pd, Rh) deposited on alumina (Al₂O₃) supports, while spent petroleum refinery hydroprocessing catalysts contain Pd, Ni, Mo, and Al. The consortium operates under acidic conditions in column bioreactors, achieving exceptional recovery rates: 93.2% Pd extraction, 82.9% Ni, 33.4% Al, and 22.7% Mo from spent petroleum catalysts. The bioleaching mechanism proceeds in two stages: (1) At. thiooxidans generates sulfuric acid that dissolves the alumina support matrix, exposing embedded PGM particles, and (2) biogenic thiosulfate (S₂O₃²⁻) produced during sulfur oxidation forms stable complexes with Pd and other PGMs in the presence of copper and ammonia, mobilizing them from the catalyst surface. The thiosulfate-copper-ammonia system enables selective PGM leaching without harsh cyanide reagents. This biotechnological approach offers an environmentally sustainable alternative to conventional pyrometallurgical PGM recovery (high-temperature smelting) and aggressive chemical leaching (aqua regia, cyanide), while addressing circular economy needs for critical materials recovery from automotive and industrial waste streams. The technology represents a significant advance in green metallurgy for spent catalyst recycling.
Taxonomy
| Taxon | Ontology ID | Functional Roles | Abundance |
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| Acidithiobacillus thiooxidans | NCBITaxon:930 · TaxonMech · TraitMech |
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Ecological Interactions
The graph shows only explicitly linked interaction participants. Community members without an asserted participant link are omitted; membership alone does not imply an interaction.
Aluminium Leaching from Refinery Catalyst
A. thiooxidans column bioleaching of an uncrushed refinery hydroprocessing catalyst released 33.4% of its Al after 315 h in submerged continuous operation. The accessible abstract reports a chemical-control kinetic fit for Al dissolution, not direct demonstration of gamma-alumina removal exposing PGM particles. This experiment is separate from synthetic Pd/alpha-alumina thiosulfate leaching; additional sulfur-oxidizing partners are not established.
Source Taxon: Acidithiobacillus thiooxidans
Metabolites: aluminium (CHEBI:28984 · MediaIngredientMech · CMMMech)
Evidence
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PMID:31059950 - SUPPORT (IN_VITRO)"about 82.9% of Ni, 33.4% of Al, and 22.7% of Mo were leached"
Biogenic Thiosulfate Leaching of Synthetic Palladium Catalyst
A separate activated-sludge gas-lift system produced up to 4.9 g/L thiosulfate at pH 10. Its liquid was concentrated at 100 C and filtered before chemical leaching of synthetic metallic Pd on alpha-alumina at 60 C, pH 8 and 5% pulp. Biogenic thiosulfate removed 93.22% of Pd from the solid, but dissolved-phase recovery was 63.53%; precipitation accounts for the discrepancy. This is not A. thiooxidans thiosulfate production, a spent-refinery PGM column, demonstrated Pt/Rh recovery, a measured unique Pd-complex stoichiometry or proof of benign industrial operation.
Metabolites: thiosulfate (CHEBI:16094 · MediaIngredientMech · CMMMech), palladium (CHEBI:33363 · MediaIngredientMech · CMMMech), copper(2+) (CHEBI:29036 · MediaIngredientMech · CMMMech), ammonia (CHEBI:16134 · MediaIngredientMech · CMMMech)
Evidence
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PMID:38138568 - SUPPORT (IN_VITRO)"with the Pd supported on alpha-alumina."
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PMID:38138568 - SUPPORT (IN_VITRO)"93.22 ± 0.06% when employing biogenic thiosulfate."
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PMID:38138568 - SUPPORT (IN_VITRO)"achieved a recovery rate in the liquid phase of 63.53 ± 0.07%"
Column Bioleaching of Refinery Catalyst Metals
Submerged continuous A. thiooxidans column operation on uncrushed spent hydroprocessing catalyst leached 82.9% Ni, 33.4% Al and 22.7% Mo after 315 h. V reached 53.6% at 105 h and then declined, consistent with precipitation; FESEM detected V in precipitates. The accessible abstract reports diffusion control for Ni and chemical control for Al/V/Mo. These are positive metal-extraction findings, not Pd/Pt/Rh recovery or a combined acid/thiosulfate cascade. Full-text conditions and mechanistic controls remain uninspected.
Source Taxon: Acidithiobacillus thiooxidans
Evidence
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PMID:31059950 - SUPPORT (IN_VITRO)"from an uncrushed petroleum refinery spent hydroprocessing catalyst using Acidithiobacillus thiooxidans"
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PMID:31059950 - SUPPORT (IN_VITRO)"The maximum yield of V (53.6%) in this column was achieved in 105 h"
Knowledge gaps & discussions (1)
KNOWLEDGE_GAP OPEN Which causal leaching steps are supported within each catalyst system separately?
The removed arrows joined distinct studies and matrices. PMID31059950 and DOI10.1016/j.jenvman.2019.04.081 are the same column article, not independent corroboration. Its abstract supports metal yields, not PGM exposure; full text remains inaccessible after publisher 403. The complete thiosulfate paper distinguishes synthetic alpha-alumina, filtered/concentrated lixiviant and solid versus liquid Pd. No coexisting supporting taxa or exact complex speciation should be invented.
Attaches to: ecological_interactions#Aluminium Leaching from Refinery Catalyst, ecological_interactions#Biogenic Thiosulfate Leaching of Synthetic Palladium Catalyst, ecological_interactions#Column Bioleaching of Refinery Catalyst Metals
1 evidence item(s)
achieved a recovery rate in the liquid phase of 63.53 ± 0.07%
Separately quantifies dissolved Pd, preserving the precipitation limitation.
Environmental Factors
| Factor | Value | Unit |
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| pH for Alumina Dissolution | 1.5-3.0 | pH |
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| Column Bioreactor Configuration | Continuous percolation | qualitative |
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| Temperature | 25-35 | °C |
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| PGM Recovery Efficiency | 93.2% Pd, 82.9% Ni, 22.7% Mo | % extraction |
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| Thiosulfate-Copper-Ammonia System | S₂O₃²⁻ + Cu²⁺/Cu⁺ + NH₃/NH₄⁺ | qualitative |
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| Substrate Type | Spent TWC and hydroprocessing catalysts | qualitative |
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