Series petroleum catalyst
Series petroleum catalyst
exacutiocatalysts principaliter includit catalyticos catalystos crepuit, hydrogenationem catalysts, catalystas reformans, etc.
• Catalytici catalysts crepuerunt aptae ad conversionem qualitatis pauperis gravis olei in leves olei et materiae rudis chemicae aptae sub variis unitatibus et processibus, sicut processu MIP-CGP, processu MIP, processu DCC, processus CPP, RTC processu, LTAG processu, FDFCC. processus MFP, processus ARGG, processus MCP, processus MGD, etc.
• Hydrogenationes catalysts pro mundatione variarum generum cibariorum olei et productorum, ut gas, pellentesque et carbones, oleum lubricatum, naphtha, cera oleum, oleum album, oleum calidum transferunt, oleum solvendum et productum sub hydrocracking, hydrorefining et residua. oleum hydrogenation augent.
• Catalysts reformantes continuas catalystas reformantes et semi-regenerantes catalystas reformantes ad productionem olei mundi luminis et aromatici cum sulphure magno octane et infimo.
Polyolefin catalysts maxime includunt polyethylenas catalystas, polypropylenas catalystas, polybutylenas catalystas, etc.
• Polyethylene catalysts ad producendum altae effectus resinae syntheticae resinae in variis processibus polyethylenis unitates et condiciones processus ut GPE processum, CX processum, Innovene G processum, Innovene S processum, Spherilene C processus bimodalis, processus Spherilene, processus Hostalen, processus Luptec G , Processus unipol, processus Bostar, Processus totalis, ADL processus slurry, processus anulus et tubus, processus anulus et tubi triplex, et aliae variae processus polyethylenae unitates et condiciones processus processus producendi summae operationis resinae syntheticae productae.
• Polypropylene catalysts ad usum in processu ST, processus SPG, processus horionis JPP, processus Hypol-Ⅱ, processus Hypol-Ⅱ, processus Innovene S, processus innovene S, processus Spheripol, processus Spherizonis, processus unipolus, processus Novolens HOEST processus, intermissus. processus corporis parvi et alius processus polypropylene plantae et processus ad producendum resinas summas perficiendi syntheticas
Calculi chemici catalystae maxime includunt SMTO methanolum ad olefin catalysts, monoxidum carbonis, synthesis oxylati catalystae oxylati et dimetril oxalati hydrogenii ad ethylenes glycol catalysts, etc. Apta sunt ad productionem olefins inferioris carbonis sicut ethylene et propylene ex methanolo.
ethylbenzene catalysts pro liquid/gas phase alkylation benzene et ethylene, isopropylbenzene catalysts pro liquido periodo alkylation benzene et propylenae, catalystae argenti pro ethylene oxidationis ad ethylene oxydi, carbonis II/III hydrogenii selectivi catalystae, titanium, siliconis catalyseos moleculares pro cribro oxydi ethylene. dehydrogenation butene, anthraquinone catalysts pro hydrogenio peroxide, oxydorum propylene catalystarum pro oxidatione propylenaeorum, C5/C6 catalystae isomerisationis alkanae, catalystae xylene isomerisation, anhydride/cis-anhydride catalystae phthalicae.phthalici/phthalici anhydridi catalystae etc. Aptae sunt ad productionem ethylene, benzene, xylene, acidi terephthalici, ethylene oxydi, ethylene glycol, styrene, acrylonitrilis, acetatis vinyl aliarumque materiarum rudium magnarum.
Environmentally amica catalystsmaxime includunt S Zorb adsorptionem desulphurisationem catalysts et SCR denitratio catalysts.
•S Zorb adsorptionem desulphurisationis catalystae, quae aptae sunt ad productionem mundi gasolini cum contento sulphuris ultra-humili et optimae retentio octanae in fractionibus sulphuris gasolini contentis.
• SCR denitrification catalysts, apta ad chemicum boiler exitum fiue gas ad consequi ultra-humilem NOx emissionem requisita
Adsorbente maxime includunt 5A sphaericum hypotheticum cribrum rorem adsorbente, p-xylene (PX) adsorbent, m-xylene (MX) adsorbent, separationem ortho-isomericam C5/C6 adsorbent, etc. Auxilia praecipue includunt gasi sulphur catalytici auxilium transferunt, crepuit catalyticum. regeneratio NOx subsidia, catalytica crepuit auxilium ad productionem propylenae augendam, summus liquor cede catalyticus crepuit auxilium, combustio auxilium etc.
• 5. Globus parva hypothetica cribro adsorbenti adsorbent, apta ad separationem n-alkanum ab iso-alkanibus et aromatibus in catena recta alkyl benzene productionis augent.
• Paraxylene (PX) adsorbent et m-xylene (MX) adsorbent, apta ad separationem altae puritatis paraxylenum et m-xylenum res e materia rudis carbonis octa-aromaticae mixtae.
•C5/C6 n-isomericae separationis adsorbenti, aptae ad continuam et efficientem separationem n-alkanum ab alkanum non-normalibus, quae praestantes compositiones gasolinarum mixturae adhibentur et n-alkanes isomerised sunt ad octanam mundi gasolini altam producendam.
• Reducendo gasi catalytici fluminum sulphuris additamenta translationis, apta ad reductionem emissionum SOx SOx in catalytico rimas regenerationis gasi.
• Catalytic crepuit regenerationem gas NOx reductionem additivam ad reductionem efficientis NOx emissiones ex catalytico rimas regenerationis fiue gas.
• catalyticus crepuit elogium ad augendum intentionem propylenae crepitationis catalyticae productae, augendae capacitatis crepitantiae olei gravis et fructus olei lucis melioris.
• Maximum liquorem praebet catalyticum crepitum additivorum, aptum ad catalyticum crepitum residua oleum in productorum liquidum valorem altum.
• Combustio auxiliorum, apta ad catalyticam rimas altam efficientiam CO combustionis imperium regenerationis dilutum tempus stabilizatio vel simultaneum NOx emissionis imperium.
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