DEVELOPMENTS IN FLUID CATALYTIC CRACKING.HEMLER CL.1976; NAFTA; JUGOSL.; DA. 1976; VOL. 27; NO 4; PP. 207-216; ABS. SERBO-CROATE RUSSEArticle

REFINERS ATTENDING NPRA SESSION SWAP EXPERIENCE WITH FCC CATALYSTS. = LES RAFFINEURS ASSISTANT A LA SESSION NPRA DISCUTENT DE LEUR EXPERIENCE CONCERNANT LES CATALYSEURS FCC1976; OIL GAS J.; U.S.A.; DA. 1976; VOL. 74; NO 12; PP. 78-82Article

NEW FCC CATALYSTS CUT ENERGY AND INCREASE ACTIVITY. = LES NOUVEAUX CATALYSEURS FCC DIMINUENT LA CONSOMMATION D'ENERGIE ET AUGMENTENT L'ACTIVITERHEAUME L; RITTER RE; BLASEK JJ et al.1976; OIL GAS J.; U.S.A.; DA. 1976; VOL. 74; NO 20; PP. 103-110 (6P.); BIBL. 16 REF.Article

FCC MODEL VALUABLE OPERATING TOOL. = LE MODELE FCC EST UN OUTIL OPERATIONNEL VALABLEWOLLASTON EG; HAFLIN WJ; FORD WD et al.1975; OIL GAS J.; U.S.A.; DA. 1975; VOL. 73; NO 38; PP. 87-94; BIBL. 7 REF.Article

FCC PROBLEMS: EROSION AND CATALYST ATTRIBUTION = PROBLEMES FCC: EROSION ET ATTRITION DU CATALYSEUR1975; OIL GAS J.; U.S.A.; DA. 1975; VOL. 73; NO 13; PP. 86-91Article

REFINERS FOCUS ON NEW FCCU TECHNOLOGY. = LES RAFFINEURS SE CONCENTRENT SUR LA NOUVELLE TECHNOLOGIE FCCU1976; OIL GAS J.; U.S.A.; DA. 1976; VOL. 74; NO 11; PP. 87-93Article

HYDROTREATING FCC FEED COULD BE PROFITABLE = L'HYDROTRAITEMENT DES CHARGES DE FCC POURRAIT ETRE RENTABLERITTER RE; BLAZEK JJ; WALLACE DN et al.1974; OIL GAS J.; U.S.A.; DA. 1974; VOL. 72; NO NO 41; PP. 99-110 (8 P.); BIBL. 7 REF.Article

FLUID CATALYTIC CRACHING PROCESS. REFINING TECHNOLOGY MODIFICATIONMIJATOVIC I.1977; NAFTA; JUGOSL.; DA. 1977; VOL. 28; NO 6; PP. 388-392; ABS. ANGL. RUSSE; BIBL. 6 REF.Article

AN OPERATIONAL APRAISAL OF FLUID CATALYTIC CRACKER WITH REGARD TO SOLID-GAS SEPARATION IN CYCLONE SYSTEMS.GOYAL OP; ALPHONSO NAX.1976; CHEM. AGE INDIA; INDIA; DA. 1976; VOL. 27; NO 2; PP. 224-273 (8P.); BIBL. 7 REF.; (SEMIN. SOLID-GAS SEP. TECH. SESS. III. PROC.; NEW DELHI; 1975)Conference Paper

CATALYST AND GAS SAMPLERS FOR FLUID CATALYTIC CRACKER REGENERATORCSICSERY SM; HARNSBERGER HF; HUGHES WD et al.1975; INDUSTR. ENGNG CHEM., PROCESS DESIGN DEVELOP.; U.S.A.; DA. 1975; VOL. 14; NO 1; PP. 93-96; BIBL. 1 REF.Article

GULF REWAMPS FCC UNITS WITH NEW PROCESS = LA GULF REAMENAGE SES UNITES FCC EN UTILISANT UN NOUVEAU PROCEDEBRYSON MC; HULING GP; GLAUSSER WE et al.1972; PETROLEUM PETROCHEM. INTERNATION.; G.B.; DA. 1972; VOL. 12; NO 9; PP. 66-72 (5 P.); BIBL. 9 REF.Serial Issue

FCC CATALYST SYSTEMS ARE TAKING NEW JOBS.1978; OIL GAS J.; U.S.A.; DA. 1978; VOL. 76; NO 15; PP. 62-70 (7P.)Article

FLUID CATALYST PROCESS. CATALYTIC CRACKING OF PETROLEUM.MURPHREE EV; BROWN CL; FISCHER HGM et al.1976; CHEM. TECH; U.S.A.; DA. 1976; VOL. 6; NO 8; PP. 523-529Article

NONLINEAR FEEDFORWARD CONTROL OF A FLUIDIZED CATALYTIC CRACKING PROCESS = COMMANDE A REACTION POSITIVE NON LINEAIRE D'UN PROCESSUS DE CRACKING CATALYTIQUE FLUIDISEENG MT; CADMAN TW; KUGELMAN AM et al.1974; I.S.A. TRANS.; U.S.A.; DA. 1974; VOL. 13; NO 3; PP. 232-252; BIBL. 29 REF.Article

MODELES STATIQUES D'OPTIMISATION DE CRAQUAGE CATALYTIQUE FLUIDEKUZNIK T.1974; INZYNIER.-CHEM.; POLSKA; DA. 1974; VOL. 4; NO 2; PP. 321-334; ABS. RUSSE ANGL.; BIBL. 1 P. 1/2Article

SULFUR DISTRIBUTION IN FCU PRODUCTS = DISTRIBUTION DU SOUFRE DANS LES PRODUITS FCUWOLLASTON EG; FORSYTHE WL; VASALOS IA et al.1971; AMER. PETROLEUM INST., PROC., DIV. REFING; U.S.A.; DA. 1971; VOL. 51; PP. 12-42; BIBL. 7 REF.; (36TH MIDYEAR MEET. AM. PET. INST. DIV. REFINING. PROC.; SAN FRANCISCO, CALIF.; 1971)Conference Paper

IMPROVING FCC OPERATIONS WITH OXYGEN ENRICHMENT = AMELIORATION DES OPERATIONS DU FCC AVEC ENRICHISSEMENT EN OXYGENEBHASIN DP; DALTON AI; PATERSON AJF et al.1982; ANNUAL FLUID CAT CRACKING SYMPOSIUM. 3/1982-05-26/AMSTERDAM; NLD; AMSTERDAM: KATALISTIKS; DA. 1982; PP. 7.1-7.37; 38 P.; BIBL. 10 REF.Conference Paper

RESID PUTS FCC PROCESS IN NEW PERSPECTIVE = LES RESIDUS OFFRENT DE NOUVELLES APPLICATIONS AU PROCEDE FCCDEAN RR; MAULEON JL; LETZSCH WS et al.1982; OIL GAS J.; ISSN 0030-1388; USA; DA. 1982; VOL. 80; NO 40; PP. 75-80; 6 P.Article

PASSIVATION OF METALS ON FCC CATALYSTS WITH ANTIMONYMCKAY DL; BERTUS BJ.1979; AMER. CHEM. SOC., DIV. PETROLEUM CHEM., PREPR.; USA; DA. 1979; VOL. 24; NO 2; PP. 645-652; BIBL. 27 REF.Article

PROCESSING EXPLORED BY Q AND A1979; HYDROCARBON PROCESSG; USA; DA. 1979; VOL. 58; NO 3; PP. 151-162Article

OFF-LINE OPTIMIZATION SYSTEM ON BELGIUM FCC UNIT PAYS OFF.BECKER SJ; HORNE EJ.1977; OIL GAS J.; U.S.A.; DA. 1977; VOL. 75; NO 52; PP. 47-51Article

USING PROCESS COMPUTERS AS ROBOTS FOR REFINING OPERATIONS = UTILISATION DES CALCULATEURS DE PROCEDE COMME ROBOTS POUR LES OPERATIONS DE RAFFINAGEKENNEDY JP.1982; HYDROCARBON PROCESS.; ISSN 0018-8190; USA; DA. 1982; VOL. 61; NO 5; PP. 160-164; BIBL. 15 REF.Article

USE OF TURBOEXPANDERS WITH FCC.MILLAR G.1978; HYDROCARBON PROCESSG; USA; DA. 1978; VOL. 57; NO 7; PP. 111-118Article

INFLUENCE DES CARACTERISTIQUES DES FUMEES SUR LA CONDUITE DES TURBINES DE RECUPERATION DANS LES UNITES DE F.C.C. = EFFECT OF SMOKE CHARACTERISTICS OF SMOKE ON OPERATING OF RECOVERY TURBINES IN FCC UNITYMALYS H.1978; INDUSTR. DU PETROLE; FRA; DA. 1978; VOL. 46; NO 494; PP. 51-56; (2 P.); ABS. ENGArticle

A CONSIDERATION OF THE TREATMENT OF COKE DISTRIBUTION IN A FLUID CATALYTIC CRACKER.SEKO H; TONE S; OTAKE T et al.1977; J. CHEM. ENGNG JAP.; JAP.; DA. 1977; VOL. 10; NO 6; PP. 493-495; BIBL. 7 REF.Article