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Results 1 to 25 of 212

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Avoid retrofit pitfalls through improved FEED : Clean fuelsESKAROS, M.Hydrocarbon processing (International ed.). 2004, Vol 83, Num 2, pp 35-37, issn 0018-8190, 3 p., 1Article

Recent developments in Chevron mild isocrackingFUCHS, M. J; POWELL, B. E; TOLBERG, R. S et al.Midyear meeting of the American Petroleum Institute's Refining Department. 49. 1984, 17 p.Conference Paper

The Calibration Report of Furfural Refining Unit in Fushun Petrochemical Company No. 1 RefineryYAN, F; CAI, Y.Petroleum science and technology. 2008, Vol 26, Num 16-18, pp 2211-2217, issn 1091-6466, 7 p.Article

Quelques résultats concernant la reconstruction de l'installation L-24-7PUTILOVA, K. L; GRIGOR'EV, N. A; OVSYANNIKOV, V. A et al.Neftepererabotka i Neftehimija (Moskva). 1984, Num 2, pp 6-8, issn 0028-1190Article

CUTBACKS IN THROUGHPUT MAY ENCOURAGE REVAMPS IN CAT-REFORMER OPERATIONS = LES REDUCTIONS DE CAPACITE PEUVENT ENCOURAGER LA MODERNISATION DES OPERATIONS DE REFORMING CATALYTIQUENAT PJ.1982; OIL GAS J.; ISSN 0030-1388; USA; DA. 1982; VOL. 80; NO 49; PP. 136-143; 4 P.Article

CHART OF DETERMINATION OF OPERATING CHARACTERISTICS OF UDO3 DESEMULSIFYING INSTALLATIONCHURIN VN.1981; NEFTEPROMYSL. DELO; ISSN 0470-6234; SUN; DA. 1981; NO 5; PP. 29-30Article

CONTROL OF DESULPHURIZATION UNITS1979; PETROLE INFORM., REV. PETROL.; FRA; DA. 1979; NO 1498; PP. 71Article

HEAVY-OIL DISTILLATION VIA COMPUTER SIMULATION.RITCHEY KJ; CANFIELD FB; CHALLAND TB et al.1976; CHEM. ENGNG; U.S.A.; DA. 1976; VOL. 83; NO 16; PP. 79-88; BIBL. 14 REF.Article

REBUILDING OF A THERMAL CRACKING FOR PETROLIUM PROCESSINGTELYASHEV GG; MARUSHKIN BK; KHURAMSHIN TZ et al.1976; NEFTEPERARAB. I NEFTEKHIM.; S.S.S.R.; DA. 1976; NO 7; PP. 30-34; BIBL. 6 REF.Article

BETTER PLANT DESIGN SAVES ENERGY. = UNE MEILLEURE CONCEPTION D'UNITE ECONOMISE L'ENERGIEDUCKHAM H; FLEMING J.1976; HYDROCARBON PROCESSG; U.S.A.; DA. 1976; VOL. 55; NO 7; PP. 78-84; BIBL. 9 REF.Article

IMPROVEMENT OF A DEWAXING SCHEME DURING PRODUCTION OF OILS FROM MANGYSHLAK OILSDEREKH PA; PODLESNAYA LA; SHELIKHOV VV et al.1978; NEFTEPERERAB. I NEFTEKHIM.; SUN; DA. 1978; NO 10; PP. 26-27Article

PRESELJENJE STARIH POGONA INA-RAFINERIJE RIJEKA NA NOVU LOKACIJU = DISPLACEMENT OF THE OLD REFINERY PLANTS TO THE NEW LOCATION. THE SELECTION OF THE METHOD FOR THE CALCULATION OF ECONOMIC EFFECTS = DEPLACEMENT DES ANCIENNES UNITES DE RAFFINAGE VERS UN NOUVEL ENDROIT. SELECTION DE LA METHODE POUR LE CALCUL DES EFFETS ECONOMIQUEOTROK A; KOLOMBO M.1977; NAFTA; YUG; DA. 1977; VOL. 28; NO 11; PP. 738-744; ABS. ENG/RUS; BIBL. 10 REF.Article

OFFSHORE PROCESS SYSTEM DESIGN REQUIRES EXACT PLANNING. = LA CONCEPTION D'UN SYSTEME DE TRAITEMENT OFFSHORE EXIGE UNE PLANIFICATION RIGOUREUSEKRYSKA TB; LINDSEY KB; HASZ JW et al.1976; OIL GAS J.; U.S.A.; DA. 1976; VOL. 74; NO 30; PP. 129-135 (3P.)Article

REBUILDING OF ELECTRIC SALT EXTRACTION INSTALLATION "ELOU 7" OF IN "OMSKNEFTSYNTEZ" PLANTUSENKO RN; ANPILOGOVA LA; ZHELETSKAYA ZA et al.1982; NEFTEPERERAB. NEFTEHIM. (MOSK.); ISSN 0028-1190; SUN; DA. 1982; NO 2; PP. 7-8Article

REFINERY ON SKIDS SPEEDS STARTUPSALTZ EX.1980; HYDROCARBON PROCESSG; USA; DA. 1980; VOL. 59; NO 5; PP. 161-164; H.T. 2Article

COMPARATIVE INDEXES OF WORKING VARIANTS OF A SECONDARY GASOLINE DISTILLATION UNITPUTILOVA KL.1978; NEFTEPERERAB. I NEFTEKHIM.; SUN; DA. 1978; NO 6; PP. 1-4Article

COMPUTER MODELING OF ALKYLATION UNITS.KNEPPER JC; KAPLAN RD; TAMPA GE et al.1977; AMER. CHEM. SOC., DIV. PETROLEUM CHEM. PREPR.; U.S.A.; DA. 1977; VOL. 22; NO 3; PP. 1040-1048; BIBL. 12 REF.Article

PARTIDA DE UNIDADE DE CRAQUEAMENTO CATALITICO ORTHOFLOW CON A FIGURA 8 DA LINHA DE TRANSFERENCIA NA POSICAO ABERTA. = PART OF A CRACKING UNIT ORTHOFLOW WITH FIGURE 8 WITH TRANSFERLINE LTO THE OPEN POSITION = PARTIE D'UNE UNITE DE CRAQUAGE CATALYTIQUE ORTHOFLOW AVEC LA FIGURE 8 DE TRANSFERT DE LIGNE EN POSITION OUVERTETEIXEIRA DE SOUZA E; FISCHER OS.1977; BOL. TEC. PETROBRAS; BRAS.; DA. 1977; VOL. 20; NO 2; PP. 101-107; ABS. ANGL.Article

HOW TO UPDATE A CATALYTIC CRACKING UNITLUCKENBACH EC.1979; CHEM. ENGNG PROGR.; USA; DA. 1979; VOL. 75; NO 2; PP. 56-61; BIBL. 2 REF.Article

FCC UNIT CONVERSION COMPLETED AT LA PAMPILLA.FRANCO A.1977; OIL GAS J.; U.S.A.; DA. 1977; VOL. 75; NO 17; PP. 104-106Article

PROCESSING EXPERIENCE OF 1A/1M INSTALLATION IN "OIL ORGANIC SYNTHESIS ANGARSK" PRODUCTION UNIONLEVIN AI; ERMAKOV EA; ZARUBIN VM et al.1979; NEFTEPERERAB. I NEFTEKHIM.; SUN; DA. 1979; NO 7; PP. 10-12Article

REBUILDING OF SECONDARY RECTIFYING INSTALLATION OF A BLIND OF SOLID PARAFFINSKITANOVA ET; TELYASHEV GG; MARUSHKIN BK et al.1976; NEFTEPERERAB. I NEFTEKHIM.; S.S.S.R.; DA. 1976; NO 7; PP. 75-78; BIBL. 2 REF.Article

Refinery Cost Functions in the U.S. Gulf CoastKAISER, M. J; GARY, J. H.Petroleum science and technology. 2009, Vol 27, Num 1-3, pp 168-181, issn 1091-6466, 14 p.Article

CONVERT TO MICROPROCESSOR CONTROLS WITHOUT SHUTDOWNLEISTER ME; SANDERS RR.1983; HYDROCARBON PROCESSING; ISSN 0018-8190; USA; DA. 1983; VOL. 62; NO 4; PP. 101-104Article

MODERNIZING OLDER STEAM CRACKERS IS PROFITABLEMOL A.1979; OIL GAS J.; USA; DA. 1979; VOL. 77; NO 14; PP. 83-96; 6 P.; BIBL. 6 REF.Article

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