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Chapter 8 Hydroprocessing and Resid Processing 2 The term resid refers to the bottom of the barrel and is usually the atmospheric tower bottoms (atmospheric reduced crude, or ARC) with an initial boiling point of 343°C or vacuum tower bottoms (vacuum reduced crude, or VRC) with an initial boiling point of 566°C. These streams contain higher concentrations of sulfur, nitrogen, and metals than does the crude oil from which they were obtained, and hydrogen/carbon ratios in the molecules are much lower. These concentrations are much higher in the case of the VRC. In the past this resid has been sold as asphalt (if the qualities of the crude permit) or as heavy fuel oil (No. 6 or bunker fuel oil). Today, more of these must be converted in the refinery to feed stocks for refining processes that will convert them to transportation fuel blending stocks. High carbon forming potentials of resids, caused by the low hydrogen/ carbon ratios in the cause rapid catalyst deactivation and high catalyst costs, and the nickel and vanadium in the resids act as catalysts for reactions creating carbon and light gaseous hydrocarbons. Catalytic processes for converting resids usually use ARC for their feedstocks, and VRC feedstocks are usually processed by noncatalytic processes. The processes most commonly used for processing ARC are reduced crude catalytic cracking units and hydroprocessing units. Thermal cracking processes such as delayed coking and Flexicoking or solvent extraction processes for VRC feedstocks. The term hydroprocessing is used to denote those processes used to reduce the boiling range of the feedstock as well as to remove substantial amounts of impurities such as 3 metals, sulfur, nitrogen, and high carbon forming compounds. COMPOSITION OF VACUUM TOWER BOTTOMS Vacuum tower bottoms are complex mixtures of high molecular weight and high boiling point compounds containing thousands of hydrocarbon and organic compounds. All of the bad processing features of refinery feedstocks are present in the bottoms streams in greater concentrations than in any of the distillate feedstocks. Because they are so complex it has been difficult to express the compositions in ways meaningful to processing operations. Liquid propane is used to extract the oil fraction from vacuum tower bottoms, and liquid n-pentane, n-hexane, or n-heptane is then used to extract the resin fraction from the residue from the propane extraction. The material insoluble in either the propane or the higher hydrocarbons is termed the asphaltene fraction. 4 Asphaltene fraction The asphaltene fraction has a very low hydrogen-to-carbon ration and consists of highly condensed ring compounds with predominating molecular weights in the 5000 to 10,000 range. The molecule is built up of sheets of these highly condensed ring structures held together by valence bonds between hetro atoms such as sulfur, oxygen, and metals. An asphaltene molecule contains three to five unit sheets consisting of condensed aromatic and naphthenic rings with paraffinic side chains. These sheets are held together by hetro atoms such as sulfur or nitrogen and/or polymethylene bridges, thioether bonds, and vanadium and nickel complexes. Separation into unit sheets is accompanied by sulfur and vanadium removal. A significant feature of the asphaltene fraction is that 80 to 90% of the metals in the crude (nickel and vanadium) are contained in this material Apparently 25 to 35% of these metals are held in porphryin structures and the remainder in some undetermined type of organic structure. The asphaltene fraction contains a higher content of sulfur and nitrogen than does the vacuum resid and also contains higher concentrations of carbon forming. 5 Hypothetical asphaltene molecule structure 6
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