High-loading Pt or Pd alloy with ZSM-5 zeolite suppresses methane formation to maximize gasoline blending component yields.
Co-feed benzene into an alkane aromatization reactor to drive transalkylation reactions that convert light aromatics into heavier C7+ hydrocarbons.
Optimized macropore architecture in solid acid catalysts extends service life and boosts trimethylpentane selectivity, resolving rapid deactivation bottlenecks.
External steam pretreatment conditions zeolite catalysts before transfer to fixed-bed reactors.
Segmenting alcohol streams allows independent olefin conversion, increasing the propylene to ethylene ratio while minimizing by-product formation.
Composite metal catalyst with sulfur addition drives dehydrogenation of dimethyltetralin isomers.
Multi-pass grids with varied openings direct catalyst flow across the reactor, preventing segregation and improving olefin production yields.
Feed pretreatment using selective adsorption removes nitrogen impurities, preventing zeolite catalyst poisoning and extending operational life.
Hydrodealkylation and transalkylation of C9 aromatic feed streams produce mesitylene and pseudocumene products.
A zeolite aromatization catalyst modified with zinc oxide, rare earth elements, and boron compounds enables efficient olefin conversion.
Microwave heating of a zeolite and metal oxide catalyst directly converts natural gas to aromatics, eliminating syngas production steps.
Layered double hydroxide composites balance acid-base sites to convert ethanol to 1,3-butadiene with high selectivity under mild conditions.
A heterogeneous catalyst system immobilizes transition metal salts on a molecular sieve support to enable efficient ethylene oligomerization.
A composite ZSM-5 molecular sieve enhances shape-selective properties through optimized pore channel ratios and controlled surface Si/Al molar ratios.
Segmented fixed bed radial flow reactor minimizes pressure drop while converting C3+ paraffins to transportable liquid aromatics.
A Zn-O-Cr binuclear site catalyst on zeolite achieves high ethylene selectivity by preventing C-C bond cleavage during ethane conversion.