convert residue to petrochemicals - World Petroleum Council

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METAL POISONING Nickel (Ni) & Vanadium (V) deposit on outer layer of catalystparticles and catalyze dehydrogenation & condensationreactions More Dry gas - can limit WGC capacity More Coke - can limit coke burning capacityHigher regn. temp.Lower cat/oil ratioLoss in conversion Ni is about four times more active than V as dehydrogenationcatalyst V has both inter & intra- particle mobility V destroys zeolite structure resulting reduced catalyst surfacearea & activity 18
Surface Area, m 2 /gMETAL POISONINGMain Contaminant metals: V, Ni, NaV - Reduces catalytic activity & enhance DG, cokeNi - Enhances DG, hydrogen, coke by dehydrogenationNa - Reduces catalytic cracking200150Ni10050VFeNa5000 10,000 15,000Metal, ppm19
Page 1 and 2: International Conference on "Refini
Page 3 and 4: MBOE/dayGLOBAL SUPPLY OF PRIMARY EN
Page 5 and 6: MB/dayGLOBAL PETROLEUM PRODUCTS DEM
Page 7 and 8: GLOBAL CRUDE QUALITY OUTLOOKo APISu
Page 9 and 10: CRUDE QUALITY SCENARIO IN 2035• S
Page 11 and 12: PROPYLENE SOURCES & DERIVATIVES306S
Page 13 and 14: GLOBAL PROPYLENE SOURCES & PRODUCTI
Page 15 and 16: RESID UPGRADATION PROCESSES• Carb
Page 17: PROBLEMS WITH RESID PROCESSING IN F
Page 21 and 22: INDMAXA breakthrough technology for
Page 23 and 24: Hardware - Simple configurationINDM
Page 25 and 26: MODE OF CATALYST REGENERATIONCoke b
Page 27 and 28: COMMERCIALIZATIONCommissioned 2000
Page 29 and 30: COLLABORATION WITH LUMMUSAgreement
Page 31 and 32: INDMAX - CONTINUAL DEVELOPMENTImpro
Page 33: SUMMARYA novel technology for direc

convert residue to petrochemicals - World Petroleum Council

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