Process for upgrading heavy hydrocarbon oils
a technology for upgrading hydrocarbons and hydrocarbon oils, which is applied in the direction of hydrocarbon oil refining, petroleum industry, liquid hydrocarbon mixture production, etc., can solve the problems of difficult to bring remote, heavy oil resources closer, and the infrastructure required for the handling, recovery and recycling of diluent could be expensiv
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example 1
Showing Typical Laboratory Process
[0042]FIG. 1 shows a process flow diagram for a laboratory unit for practicing some embodiments of the invention. Oil and supercritical water are contacted in a mixer prior to entering the reactor. The reactor is equipped with an inner tube for collecting the products (syncrude, excess water, and gas), and a bottom section where any metals or solids comprising a “dreg stream” of indeterminate properties or composition may accumulate. The shell-side of the reactor is kept isothermal during the reaction with a clamshell furnace and temperature controller. Preferred reactor residence times are 20-40 minutes, with preferred oil / water volume ratios on the order of 1:3. Preferred temperatures are around 374°-400° C. with the pressure at 3,200-4,000 psig. The reactor product stream leaves as a single phase, and is cooled and separated into gas, syncrude, and effluent water. The effluent water is recycled back to the reactor. Sulfur from the original feedst...
example 2
Properties of the Product Syncrude
[0044]A Hamaca crude oil was diluted with a diluent hydrocarbon at a ratio of 5:1 (20 vol % of diluent). The diluted Hamaca crude oil properties were measured before reacting it with the supercritical water process as referred to in Example 1 and FIG. 2. The properties of the crude were as follows: 12.8 API gravity at 60 / 60; 1329 CST viscosity @40° C.; 7.66 wt % C / H ratio; 13.04 wt % MCRT; 3.54 wt % sulfur; 0.56 wt % nitrogen; 3.05 mg KOH / gm acid number; 1.41 wt % water, 371 ppm Vanadium; and 86 ppm Nickel. The diluted Hamaca crude oil after the super critical water treatment was converted into a syncrude with the following properties: 24.1 API gravity at 60 / 60; 5.75 CST viscosity @40° C.; 7.40 wt % C / H ratio; 2.25 wt % MCRT; 2.83 wt % sulfur; 0.28 wt % nitrogen; 1.54 mg KOH / gm acid number; 0.96 wt % water; 24 ppm Vanadium; and 3 ppm Nickel Substantial reductions in metals and residues were observed, with simultaneous increase in the API gravity and...
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