Hydrogen shale oil

The shale oil produced is a viscous material that required hydrogenation to eliminate sulfur, nitrogen, and oxygen, to reduce its viscosity, and to Improve its stability. The hydrogenation will be done at the production site to improve the properties of the shale oil before pipelining to a refinery. Hydrogenated shale oil is a reasonable substitute for crude oil, and still requires refining. 

Petroleum, particulady shale oil, also contains organic oxygen and nitrogen compounds. Model reactions for the removal of these materials with hydrogen include... 

Shale oil contains large quantities of olefinic hydrocarbons (see Table 8), which cause gumming and constitute an increased hydrogen requirement for upgrading. Properties for cmde shale oil are compared with petroleum cmde in Table 10. High pour points prevent pipeline transportation of the cmde shale oil (see Pipelines). Arsenic and iron can cause catalyst poisoning. 

Utilisa tion of shale oil products for petrochemical production has been studied (47—51). The effects of prerefining on product yields for steam pyrolysis of shale oil feed and the suitabiUty of Green River shale oil as a petrochemical feedstock were investigated. Pyrolysis was carried out on the whole oil, vacuum distillate, and mildly, moderately, and severely hydrogenated vacuum distillates. 

Detergents have been manufactured from long-chain alkenes and sulfuhc acid, especially those obtained from shale oil or cracking of petroleum wax. These are sulfated with 90—98 wt % acid at 10—15°C for a 5-min contact time and at an acid—alkene molar ratio of 2 1 (82). Dialkyl sulfate initially forms when 96 wt % acid is added to 1-dodecene at 0°C, but it is subsequently converted to the hydrogen sulfate in 80% yield upon the further addition of sulfuhc acid. The yield can be increased to 90% by using 98 wt % sulfuhc acid and pentane as the solvent at -15°C (83). 

Ahlborg G. 1951. Hydrogen sulfide poisoning in shale oil industry. Arch Ind Hyg Occup Med 3 247-266. 

Statfjord atmospheric resid (1). Atmospheric resid (2). SRC II (3). Prahoe shale oil (4). Directly liquefied oil from wood chips using the PERC process (5). Molar ratio adjusted assuming that ammonia, water and hydrogen sulfide are formed by the heteroatoms. 

The chief examples are smelting for the recovery of metals from ores, cement manufacture, and lime burning. The converters, roasters, and kilns for these purposes are huge special devices, not usually adaptable to other chemical applications. Shale oil is recovered from crushed rock in a vertical kiln on a batch or continuous basis—moving bed in the latter case—sometimes in a hydrogen-rich atmosphere for simultaneous denitrification and desulfurization. The capacity of ore roasters is of the order of 300-700 tons/(day)(m3 of reactor volume). Rotary kilns for cement have capacities of 0.4-1.ltons/(day)(m3) for other purposes the range is 0.1-2. 

Oil - [COALCONVERSIONPROCESSES - CARBONIZATION] (Vol6) - [COALCONVERSIONPROCESSES - GASIFICATION] (Vol6) - [SIZE ENLARGEMENT] (Vol 22) -fuel for limestone kilns [LIME AND LIMESTONE] (Vol 15) -hydrogen from [HYDROGEN] (Vol 13) -measurement of particles m [SIZE MEASUREMENT OF PARTICLES] (V ol 22) -m nuts [NUTS] (Vol 17) -as petroleum lubricant [LUBRICATION AND LUBRICANTS] (Vol 15) -pipeline transport [PIPELINES] (Vol 19) -sample analysis by ms [MASS SPECTROMETRY] (Vol 15) -from shale [OIL SHALE] (Vol 17) -steel quenching m [STEEL] (Vol 22) -sulfur removal from [SULFUR] (Vol 23) -tanks for [TANKS AND PRESSURE VESSELS] (Vol 23) -use of fluidization [FLUIDIZATION] (Vol 11)... 

The synthetic crude was produced by hydrogenating the IBP-350°F naphtha, the 350°-550°F light oil, and the 550°-850°F heavy oil fractions obtained from in situ crude shale oil by distillation followed by coking of the 850°F-f- residuum. Characterization of the syncrude was accomplished by examining the following fractions CB-175°F light naphtha, 175°-350°F heavy naphtha, 350°-550°F light oil, and 550°-850°F heavy oil. 

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