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Petroleum Refinery Process : DESCRIPTION AND HISTORY

                 PETROLEUM  REFINERY PROCESS: DESCRIPTION AND HISTORY    



              Petroleum refining has evolved continuously in response to changing consumer demand for better and different products. The original requirement was to produce kerosene as a cheaper and better source of light than whale oil. The development of the internal combustion engine led to the production of gasoline and diesel fuels. The evolution of the airplane created a need first for high-octane aviation gasoline and then for jet fuel, a sophisticated form of the original product, kerosene. Present-day refineries produce a variety of products including many required as feedstock for the petrochemical industry.
1. Distillation Processes. The first refinery, opened in 1861, produced kerosene by simple atmospheric distillation. Its by-products included tar and naphtha. It was soon discovered that high-quality lubricating oils could be produced by distilling petroleum under vacuum. However, for the next 30 years kerosene was the product consumers wanted. Two significant events changed this situation: (1) invention of the electric light decreased the demand for kerosene, and (2) invention of the internal combustion engine created a demand for diesel fuel and gasoline (naphtha).
2. Thermal Cracking Processes. With the advent of mass production and World War I, the number of gasoline-powered vehicles increased dramatically and the demand for gasoline grew accordingly. However, distillation processes produced only a certain amount of gasoline from crude oil. In 1913, the thermal cracking process was developed, which subjected heavy fuels to both pressure and intense heat, physically breaking the large molecules into smaller ones to produce additional gasoline and distillate fuels. Visbreaking, another form of thermal cracking, was developed in the late 1930's to produce more desirable and valuable products.
3. Catalytic Processes. Higher-compression gasoline engines required higher-octane gasoline with better antiknock characteristics. The introduction of catalytic cracking and polymerization processes in the mid- to late 1930's met the demand by providing improved gasoline yields and higher octane numbers.
Alkylation, another catalytic process developed in the early 1940's, produced more high-octane aviation gasoline and petrochemical feedstock for explosives and synthetic rubber. Subsequently, catalytic isomerization was developed to convert hydrocarbons to produce increased quantities of alkylation feedstock. Improved catalysts and process methods such as hydrocracking and reforming were developed throughout the 1960's to increase gasoline yields and improve antiknock characteristics. These catalytic processes also produced hydrocarbon molecules with a double bond (alkenes) and formed the basis of the modern petrochemical industry.

4. Treatment Processes. Throughout the history of refining, various treatment methods have been used to remove nonhydrocarbons, impurities, and other constituents that adversely affect the properties of finished products or reduce the efficiency of the conversion processes. Treating can involve chemical reaction and/or physical separation. Typical examples of treating are chemical sweetening, acid treating, clay contacting, caustic washing, hydrotreating, drying, solvent extraction, and solvent dewaxing. Sweetening compounds and acids desulfurize crude oil before processing and treat products during and after processing.
Following the Second World War, various reforming processes improved gasoline quality and yield and produced higher-quality products. Some of these involved the use of catalysts and/or hydrogen to change molecules and remove sulfur. A number of the more commonly used treating and reforming processes are described in this chapter of the manual.

                                                     HISTORY OF REFINING
Year


Process name


Purpose


By-products, etc.


1862 Atmospheric distillation Produce kerosene Naphtha, tar, etc.
1870 Vacuum distillation Lubricants (original)
Cracking feedstocks (1930's)
Asphalt, residual
coker feedstocks
1913 Thermal cracking Increase gasoline Residual, bunker fuel
1916 Sweetening reduce sulfur & odor Sulfur
1930 Thermal reforming Improve octane number Residual
1932 Hydrogenation Remove sulfur Sulfur
1932 Coking Produce gasoline basestocks Coke
1933 Solvent extraction Improve lubricant viscosity index Aromatics
1935 Solvent dewaxing Improve pour point Waxes
1935 Cat. polymerization Improve gasoline yield
& octane number
Petrochemical
feedstocks
1937 Catalytic cracking Higher octane gasoline Petrochemical
feedstocks
1939 Visbreaking reduce viscosity Increased distillate,tar
1940 Alkylation Increase gasoline octane & yield High-octane aviation gasoline
1940 Isomerization Produce alkylation feedstock Naphtha
1942 Fluid catalytic cracking Increase gasoline yield & octane Petrochemical feedstocks
1950 Deasphalting Increase cracking feedstock Asphalt
1952 Catalytic reforming Convert low-quality naphtha Aromatics
1954 Hydrodesulfurization Remove sulfur Sulfur
1956 Inhibitor sweetening Remove mercaptan Disulfides
1957 Catalytic isomerization Convert to molecules with high octane number Alkylation feedstocks
1960 Hydrocracking Improve quality and reduce sulfur Alkylation feedstocks
1974 Catalytic dewaxing Improve pour point Wax
1975 Residual hydrocracking Increase gasoline yield from residual Heavy residuals

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