The Catalytic Refinery (1940-1970)

The Catalytic Refinery (1940-1970) azs2

As discussed in Lessons 6 and 7, the development of catalytic processes has changed the chemistry of petroleum refining from free radical to ionic reactions. World War II provided the stimulus to urgently develop catalytic technologies that were being investigated in the late thirties. The catalytic age of refining, which could be bracketed between1940 and 1970 also brought the advent of the petrochemical industry.

Figure 11.5 shows a configuration of the catalytic refinery which resembles, to a large extent, the current day refineries focused on making high yields of gasoline. The introduction of catalytic cracking, reforming, alkylation, polymerization has revolutionized the ways of making high octane number gasoline. Development of hydrotreatment processes was also an important asset of the catalytic refinery. Hydrotreatment was essential to protect the platinum catalyst used in reforming from sulfur and as a versatile finishing process to replace the chemical treatments used in the thermal refinery to finish fuels.

Configuration of catalytic refinery 1940-1970. For key information see surrounding text.
Figure 11.5. The configuration of the catalytic refinery [4].
 

One should note in Figure 11.5 that the catalytic refinery also incorporated new thermal processes such as delayed coking and visbreaking, and separation processes, such as deasphalting. Principles of chemical engineering have found great applications in the development of the catalytic refinery with particular emphasis on designing different catalytic process configurations (remember Fixed-Bed, Moving-Bed, and Fluid-Bed Catalytic Cracking), catalyst development, thermal efficiency (e.g., FCC) and product yield and selectivity. The catalytic refinery produced large quantities of LPG (for reasons discussed in Lesson 7) and witnessed the increasing demand for kerosene, now as jet fuel. The time-line for the development of refining processes shown in Table 11.1 shows the intense activity of process development, particularly during World War II.

The age of catalytic refining may be considered to have ended in the 1970s, not because new chemistry was introduced, as it happened in the transition from thermal to catalytic refinery or the development of new process concepts. The oil crises of the 1970s highlighted the significance of refinery flexibility with respect to the diversity of crude oil slates. Further, the concerns for environmental pollution by the combustion of petroleum fuels have brought emphasis on more effective finishing processes. These factors lead to the development of the modern refinery focused on processing the heavy ends of petroleum and making cleaner fuels.

Table 11.1. Historical time-line for petroleum refining processes [6].
YearProcess NamePurposeByproducts, etc. 
1849Canadian geologist Abraham Gesner distills kerosine from crude oil
1859An oil refinery is built in Baku (Azerbaijan)
1860-1861Oil refineries are built near Oil Creek, Pennsylvania; Petrolia, Ontario, Canada; and Union County, Arkansas
1862Atmosphere distillationProduce kerosineNaphtha, tar, etc. 
1870Vacuum distillationLubricants (original) cracking feedstocks (1930s)Asphalt, residual coker feedstocks
1913Thermal CrackingIncrease gasolineResidual, bunker fuel
1916SweeteningReduce sulfur and odorSulfur
1930Thermal reformingImprove octane numberResidual
1932HydrogenationRemove sulfurSulfur
1932CokingProduce gasoline base stocksCoke
1933Solvent extractionImprove lubricant viscosity indexAromatics
1935Solvent dewaxingImprove pour pointWaxes
1935Catalyst polymerizationImprove gasoline yield and octane numberPetrochemical feedstocks
1937Catalytic crackingHigher octane gasolinePetrochemical feedstocks
1939VisbreakingReduce viscosityIncreased distillate, tar
1940AlkylationIncrease gasoline octane and yieldHigh-octane aviation gasoline
1940IsomerizationProduce alkylation feedstockNaphtha
1942Fluid catalytic crackingIncrease gasoline yield and octanePetrochemical feedstocks
1950DeasphaltingIncrease cracking feedstockAsphalt
1952Catalytic reformingConvert low-quality naphthaAromatic
1954HydrodesulfurizationRemove sulfurSulfur
1956Inhibitor sweeteningRemove mercaptanDisulfides
1957Catalytic isomerizationConvert to molecules with high octane numberAlkylation feedstocks
1960HydrocrackingImprove quality and reduce sulfurAlkylation feedstocks
1974Catalytic dewaxingImprove pour pointWax
1975Residual hydrocrackingIncrease gasoline yield from residualHeavy residuals
1975Catalytic converterThe phaseout of tetraethyl lead beginsCleaner air
1990sSCANfining (Exxon), OCTGAIN (Mobil), Prime G (Axens), and S Zorb (Phillips)Reformulated gasoline and low-sulfur dieselLow sulfur fuel
2000Deep or ultra-deep desulfurization (ULSD)Decrease sulfur level in diesel (2 ppm0Sulfur

 

[4.] F. Self, E. Ekholm, and K. Bowers, Refining Overview - Petroleum, Processes and Products, AIChE, 2000, Chapter 6. [6.] M.R. Riazi, S. Eser2, J. L. Peña Díez, and S. S. Agrawal, “Introduction” In Petroleum Refining and Natural Gas Processing, Editors: M. R. Riazi, S. Eser, J. L. Peña, S. S. Agrawal, ASTM International, West Conshohocken, PA, 2013, p.6