Solvent deasphalting apparatus

Claim 1

An apparatus useful for solvent deasphalting black oils which comprises: (a) a vertically oriented vessel having an internal volume formed by a cylindrical side wall which has an internal surface, the vessel being divided into an upper section and a lower section and having upper and lower ends; (b) a solvent inlet means communicating with the internal volume of the vessel at a first point in the lower section of the vessel and above the lower end of the vessel; (c) a charge stock inlet means communicating with the internal volume of the vessel at a higher second point in the vessel; (d) a first plurality of vertically spaced apart and substantially horizontal liquid-liquid contacting trays located within the vessel above the solvent inlet means and below the charge stock inlet means; (e) an indirect heat exchange means located in the upper section of the vessel above the charge stock inlet means and comprising a first and a second bundle of horizontal U-shaped heat exchange tubes which extend across the internal volume of the vessel, each bundle passing through the side wall at only one point, with this point being on the opposite side of the vessel from the point at which the other bundle passes through the side wall and at the same vertical elevation, the two bundles being positioned adjacent each other; (f) a second plurality of vertically spaced apart and substantially horizontal liquid-liquid contacting trays located within the vessel above the charge stock inlet means and below the indirect heat exchange means; (g) a first liquid outlet means communicating with the internal volume of the vessel at the upper end of the vessel, and a second liquid outlet means communicating with the internal volume of the vessel at the lower end of the vessel; (h) a substantially imperforate horizontal shroud operably positioned above the indirect heat exchange means, the longitudinal axis of the shroud being in alignment with the longitudinal axis of the first and the second bundles of heat exchange tubes, the shroud having two opposing curved edges which abut the internal surface of the side wall at points directly above the intersection of the heat exchange means with the side wall, the shroud also having two parallel and opposing substantially straight edges which extend between the curved edge, with the straight edges being separated by a distance greater than the combined width of the two heat exchange bundles, and thereby providing for vertical liquid flow two opposing chordal openings in the cross-section of the vessel defined by the straight edges of the shroud and the internal surface of the side wall; (i) a first pair of chordal liquid baffle plates located within the vessel above the shroud, the first pair of plates being operably positioned on opposing sides of the side wall at points directly above the two chordal openings in the cross-section of the vessel defined by the shroud, with each baffle plate having a curved edge which abuts the internal surface of the side wall and a straight edge which is parallel to the straight edges of the shroud, the vertical distance between the first pair of baffle plates and the upper end of the vessel being greater than the radius of the vessel, with the internal volume of the vessel above the first pair of baffle plates being devoid of structural components which extend across the cross-section of the vessel; and, (j) a second pair of chordal liquid baffle plates located within the vessel, the second pair of plates being operably positioned on opposing sides of the side wall at points directly below the two chordal openings in the cross-section of the vessel defined by the shroud, each baffle plate having a curved edge which abuts the internal surface of the side wall and a straight edge which is parallel to the straight edges of the shroud, the straight edge of each baffle plate being located below a horizontal centerline through the first and second bundle heat exchange tubes, whereby a stream of solvent may be fed to the lower section of the vessel through the solvent inlet means to countercurrently contact a black oil stream charged through the charge stock inlet means in the first plurality of contacting trays and then to countercurrently contact a second liquid phase in the second plurality of contacting trays, with the resulting extract stream being caused to pass upward through the heat exchange means by the action of the second pair of baffle plates and admixed to a uniform temperature by the action of the shroud and the first pair of baffle plates, with the extract stream then being retained within a quiescent settling zone above the first pair of baffle plates before being discharged from the vessel.

Claim 2

An apparatus useful for solvent deasphalting black oils which comprises: (a) a vertically oriented vessel having an internal volume formed by a cylindrical side wall which has an internal surface, the vessel being divided into an upper section and a lower section and having upper and lower ends; (b) a solvent inlet means communicating with the internal volume of the vessel at a first point in the lower section of the vessel and above the lower end of the vessel; (c) a charge stock inlet means communicating with the internal volume of the vessel at a higher second point in the vessel; (d) a first plurality of vertically spaced apart and substantially horizontal liquid-liquid contacting trays located within the vessel above the solvent inlet means and below the charge stock inlet means; (e) an indirect heat exchange means located in the upper section of the vessel above the charge stock inlet means and comprising a first and a second bundle of horizontal U-shaped heat exchange tubes which extend across the internal volume of the vessel, each bundle passing through the side wall at only one point, with this point being on the opposite side of the vessel from the point at which the other bundle passes through the side wall and at the same vertical elevation, the two bundles being positioned adjacent each other; (f) a second plurality of vertically spaced apart and substantially horizontal liquid-liquid contacting trays located within the vessel above the charge stock inlet means and below the indirect heat exchange means; (g) a first liquid outlet means communicating with the internal volume of the vessel at the upper end of the vessel, and a second liquid outlet means communicating with the internal volume of the vessel at the lower end of the vessel; (h) a substantially imperforate horizontal shroud operably positioned above the indirect heat exchange means, the longitudinal axis of the shroud being in alignment with the longitudinal axis of the first and the second bundles of heat exchange tubes, the shroud having two opposing curved edges which abut the internal surface of the side wall at points directly above the intersection of the heat exchange means with the side wall, the shroud also having two parallel and opposing substantially straight edges which extend between the curved edge, with the straight edges being separated by a distance greater than the combined width of the two heat exchange bundles, and thereby providing for vertical liquid flow two opposing chordal openings in the cross-section of the vessel defined by the straight edges of the shroud and the internal surface of the side wall; (i) a first pair of chordal liquid baffle plates located within the vessel above the shroud, the first pair of plates being operably positioned on opposing sides of the side wall at points directly above the two chordal openings in the cross-section of the vessel defined by the shroud, with each baffle plate having a curved edge which abuts the internal surface of the side wall and a straight edge which is parallel to the straight edges of the shroud, the vertical distance between the first pair of baffle plates and the upper end of the vessel being greater than the radius of the vessel, with the internal volume of the vessel above the first pair of baffle plates being devoid of structural components which extend across the cross-section of the vessel; and, (j) a second pair of chordal liquid baffle plates located within the vessel, the second pair of plates being operably positioned on opposing sides of the side wall at points directly below the two chordal openings in the cross-section of the vessel defined by the shroud, each baffle plate having a curved edge which abuts the internal surface of the side wall and a straight edge which is parallel to the straight edges of the shroud, the straight edge of each baffle plate being located below a horizontal centerline through the first and second bundle heat exchange tubes, whereby a stream of solvent may be fed to the lower section of the vessel through the solvent inlet means to countercurrently contact a black oil stream charged through the charge stock inlet means in the first plurality of contacting trays and then to countercurrently contact a second liquid phase in the second plurality of contacting trays, with the resulting extract stream being caused to pass upward through the heat exchange means by the action of the second pair of baffle plates and admixed to a uniform temperature by the action of the shroud and the first pair of baffle plates, with the extract stream then being retained within a quiescent settling zone above the first pair of baffle plates before being discharged from the vessel.