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Results 1 to 25 of 150

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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

Empresas de ingenieria : obras y progectos en curso = Engineering firms : works and projects on handOilgas. 2000, Vol 33, Num 380, pp 50-75, issn 0030-1493, 13 p.Article

Los proyectos en curso en las refinerías españolas suponen una inversión de 100.000 millones de pesetas = Outstanding projects in spanish refineries imply 100.000 millions pesetas investmentOilgas. 1998, Vol 31, Num 362, pp 15-21, issn 0030-1493, 4 p.Article

Choosing methods for industrial hydrocarbon refiningBUDNIKOV, V. F; MYASISHCHEV, YU. G; SHACHIN, A. A et al.Chemical and petroleum engineering. 1996, Vol 32, Num 6, pp 537-539, issn 0009-2355Article

Dynamic modeling and simulation of a catalytic cracking unitZHENG, Y.-Y.Computers & chemical engineering. 1994, Vol 18, Num 1, pp 39-44, issn 0098-1354Article

Datis de la actinidad de las compañas españolas: CEPSA, REPSOL PETRÓLEO, ERTOIL, PETROMED, PETRONOR y ASESA = Statistic data of the spanish oil companies activity: CEPSA, REPSOL PETRÓLEO, ERTOIL, PETROMED, PETRONOR and ASESAOilgas. 1991, Vol 24, Num 284, pp 29-58, issn 0030-1493, 20 p.Article

Changing timesSHARGAY, C. A; SMITH, A. R.Hydrocarbon engineering. 2003, Vol 8, Num 8, pp 27-31, issn 1468-9340, 5 p.Article

Instalaciones de almacenamiento de productos petroliferos en España = Petroleum product storage equipement in SpainOilgas. 1998, Vol 31, Num 360, pp 25-40, issn 0030-1493, 8 p.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

Inversiones en torno a los 400.000 millones de pesetas hasta el 2002 en el sector quιmico/petroquιmico en España = About 400.000 millions pesetas investments for chemical and petrochemical industries in Spain until 2002Oilgas. 1997, Vol 30, Num 354, pp 24-29, issn 0030-1493, 5 p.Article

La industria del refino en España = Refining industry in SpainOilgas. 2000, Vol 33, Num 384, issn 0030-1493, 61Article

Moderate-temperature isomerizate A high-octane component ofautomotive gasolineATARSHCHIKOV, S. V; MIRIMANYAN, A. A; MKRTYCHEV, A. A et al.Chemistry and technology of fuels and oils. 2005, Vol 41, Num 5, pp 362-369, issn 0009-3092, 8 p.Article

La industria del refino en España. Datos estadísticos de la actividad en 1997 de las compañias refinadoras españolas : CEPSA, REPSOL, BP Oil España, PETRONOR y ASESA = Refining industry in Spain. Statistics of 1997 activity of spanish refining companies : CEPSA, REPSOL, BP Oil España, PETRONOR and ASESAOilgas. 1998, Vol 31, Num 362, pp 23-52, issn 0030-1493, 20 p.Article

Maintaining peak performance in fiexed bed hydroprocessing unitsLOUREIRO, R. C.SPE 1990 latino-american petroleum engineering conference4° congreso brasileiro de petróleo. 1990, pp 01-18Conference Paper

Fortune tellerHENDERSON, Peter; HAZLETT, John; SCHINDLER, Henry et al.Hydrocarbon engineering. 2003, Vol 8, Num 5, pp 103-106, issn 1468-9340, 3 p.Article

Modernization of the vacuum section in the EDU-AVT-3 unitPOPOV, V. G; KOBAK, O. A; FILIMONOV, I. V et al.Chemistry and technology of fuels and oils. 2000, Vol 36, Num 3, pp 195-198, issn 0009-3092Article

Online optimization : What have we learned?WHITE, D. C.Hydrocarbon processing (International ed.). 1998, Vol 77, Num 6, pp 55-59, issn 0018-8190Article

Planta de platformado en la refinería de Algeciras de Cepsa = Platforming plant in Cepsa refinery in AlgecirasOilgas. 1997, Vol 30, Num 355, pp 5-17, issn 0030-1493, 8 p.Article

Experience in initial operation of cat cracking section in G-43-107M/1 combination unitEGOROV, I. V; GANTSEV, V. A; MELIK-AKHNAZAROV, T. KH et al.Chemistry and technology of fuels and oils. 1996, Vol 32, Num 6, pp 294-299, issn 0009-3092Article

Prince, a knowledge-based system to assist process developmentWAHL, F.Computers & chemical engineering. 1994, Vol 18, pp S171-S175, issn 0098-1354, SUPConference Paper

Improving yields of conversion unit feedstocks with VDU deep-cutJOHNSON, E. K.SPE 1990 latino-american petroleum engineering conference4° congreso brasileiro de petróleo. 1990, pp 01-13Conference Paper

L'intensification du processus de cokéfaction différée lors du passage à un schéma sans recirculationFEDOTOV, V. E; GIMAEV, R. N; VALYAVIN, G. G et al.Neftepererabotka i Neftehimija (Moskva). 1988, Num 8, pp 3-6, issn 0028-1190Article

Evaluation rapide du coût d'un investissement: méthode des modules fonctionnels = Quick evaluation of investment cost: the functional module methodCHAUVEL, A; BENCHECROUN, N; RAIMBAULT, C et al.Revue de l'Institut français du pétrole. 1987, Vol 42, Num 4, pp 465-480, issn 0020-2274Article

Review fundamentals when retrofitting for ULSD : Clean fuelsPALMER, R. E; JOHNSON, J. W.Hydrocarbon processing (International ed.). 2004, Vol 83, Num 2, pp 39-41, issn 0018-8190, 3 p., 1Article

Integrating refining and petrochemicalsMA'ADHAH, A; ABDUL-HAMAYEL, M; REDHWI, H et al.Hydrocarbon engineering. 2003, Vol 8, Num 6, pp 49-54, issn 1468-9340, 4 p.Article

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