LEADER 03333nam 2200697Ia 450 001 9910818406203321 005 20200520144314.0 010 $a1-04-005265-7 010 $a0-429-06682-1 010 $a1-4398-8046-8 024 7 $a10.1201/b13879 035 $a(CKB)2670000000327159 035 $a(EBL)1114014 035 $a(OCoLC)827209664 035 $a(SSID)ssj0000873708 035 $a(PQKBManifestationID)11435841 035 $a(PQKBTitleCode)TC0000873708 035 $a(PQKBWorkID)10877499 035 $a(PQKB)11104279 035 $a(Au-PeEL)EBL1114014 035 $a(CaPaEBR)ebr10648170 035 $a(CaONFJC)MIL693345 035 $a(OCoLC)826413449 035 $a(PPN)184237726 035 $a(CaSebORM)9781439880456 035 $a(MiAaPQ)EBC1114014 035 $a(OCoLC)1280139758 035 $a(FINmELB)ELB145268 035 $a(EXLCZ)992670000000327159 100 $a20111102d2013 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 10$aModeling of processes and reactors for upgrading of heavy petroleum /$fJorge Ancheyta 205 $a1st ed. 210 $aBoca Raton $cCRC/Taylor & Francis$d2013 215 $a1 online resource (551 p.) 225 0 $aChemical industries ;$v136 300 $aDescription based upon print version of record. 311 $a1-322-62063-6 311 $a1-4398-8045-X 320 $aIncludes bibliographical references. 327 $aFront Cover; Contents; Preface; Acknowledgments; Author; Chapter 1 - Heavy Petroleum; Chapter 2 - Technologies for Upgrading of Heavy Petroleum; Chapter 3 - Modeling of Visbreaking; Chapter 4 - Modeling of Gasification; Chapter 5 - Modeling of Coking; Chapter 6 - Noncatalytic (Thermal) Hydrotreating; Chapter 7 - Modeling of Catalytic Hydroprocessing; Chapter 8 - Modeling and Simulation of Heavy Oil Hydroprocessing; Chapter 9 - Modeling of Bench-Scale Reactor for HDM and HDS of Maya Crude Oil; Chapter 10 - Modeling of Ebullated-Bed and Slurry-Phase Reactors 327 $aChapter 11 - Modeling of Hydrocracking by Continuous Kinetic Lumping ApproachChapter 12 - Correlations and Other Aspects of Hydroprocessing; Back Cover 330 $aThe worldwide petroleum industry is facing a dilemma: the production level of heavy petroleum is higher than that of light petroleum. Heavy crude oils possess high amounts of impurities (sulfur, nitrogen, metals, and asphaltenes), as well as a high yield of residue with consequent low production of valuable distillates (gasoline and diesel). These characteristics, in turn, are responsible for the low price of heavy petroleum. Additionally, existing refineries are designed to process light crude oil, and heavy oil cannot be refined to 100 percent. One solution to this problem is the installatio 410 0$aChemical Industries 606 $aPetroleum$xRefining 606 $aPetroleum industry and trade 615 0$aPetroleum$xRefining. 615 0$aPetroleum industry and trade. 676 $a546.434 700 $aAncheyta Juarez$b Jorge$0915445 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910818406203321 996 $aModeling of processes and reactors for upgrading of heavy petroleum$94081299 997 $aUNINA