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The thermal cracking process functioned largely in accordance with the free-radical theory of molecular transformation.
…American chemist who developed a thermal cracking process for increasing the proportion of gasoline obtainable from petroleum.
He developed a version of the widely used thermal cracking process for refineries, which increased gasoline yield.
About 1910 Standard Oil (Indiana) developed the first thermal cracking process, which became an important method for producing larger quantities of high-octane gasoline from petroleum.
During service, the tube inner surfaces were operated at temperature in the range of 820 835 °C within which thermal cracking process occurred.
The first thermal cracking process for breaking up large nonvolatile hydrocarbons into gasoline came into use in 1913; it was invented by William Merriam Burton, a chemist who worked for the Standard Oil Company (Indiana), which later became the Amoco Corporation.
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The thermal cracking processes developed for refinery processing in the 1920s were focused primarily on increasing the quantity and quality of gasoline components.
Such kinds of hydrocarbon-based nanofluids may have the potential to reach higher heat sink values during their thermal cracking processes due to the catalytic effects of Au NPs.
With the study object of an 100kt/a SL-II ethylene cracking furnace, this paper used Computational Fluid Dynamics (CFD) method to carry out coupled simulation studies on the flow, combustion, radiative heat transfer and thermal cracking reaction processes in the cracking furnace.
A mathematical model for catalyst regenerator of fluidized bed catalytic cracking process, including thermal effects, has been developed to simulate a regenerator having characteristics similar to that of the unit operated by Petrobras (Brazilian Oil Company).
It has been well-established that both thermal cracking and catalytic cracking can generate dry gas.
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