ATOMIZING NOZZLE AND METHOD OF USE THEREOF

    公开(公告)号:JPH11262702A

    公开(公告)日:1999-09-28

    申请号:JP2194999

    申请日:1999-01-29

    Applicant: MOBIL OIL CORP

    Abstract: PROBLEM TO BE SOLVED: To provide a nozzle capable of carrying out a favorable shearing function at a feed speed of a dispersed hydrocarbon and mixing droplets of the fed hydrocarbon and catalyst. SOLUTION: This nozzle comprises (a) a nozzle barrel 2 having a center long axis, an inlet end part, and a tip end part; (b) a tip 14 having a vertical center axis, the inner surface, and an outer surface and which is to be connected with the tip end part of the nozzle barrel 2; and (c) at least three apertures extended from the inner side surface of the tip 14 to the outside surface. Each aperture part has the length longer than the width, further has a center long axis constituted of a first middle point of the inner side surface 137 of the tip 14, a second middle point in the outer surface 135 of the tip 14, and a line transversely crossing the first and the second middle points. The angle θ formed between the center long axis of each aperture part and the center long axis of the nozzle barrel 2 is from zero to about 75 deg.. Such a nozzle is used as an atomizing nozzle.

    PRODUCTION OF HIGH-VISCOSITY-INDEX LUBRICANT

    公开(公告)号:JPH0665584A

    公开(公告)日:1994-03-08

    申请号:JP14342993

    申请日:1993-06-15

    Applicant: MOBIL OIL CORP

    Abstract: Petroleum wax feeds are converted to high Viscosity Index lubricants by a two-step hydrocracking-hydroisomerization process in which the wax feed is initially subjected to hydrocracking under mild conditions with a conversion to non-lube range products of no more than 30 weight percent of the feed. The hydrocracking is carried out at a hydrogen pressure of at least 7000 kPa (1000 psig) using an amorphous catalyst which preferentially removes the aromatic components present in the initial feed. The hydrocracked effluent is then subjected to hydroisomerization in a second step using a low acidity dicarboxylic acid-treated zeolite Beta or mordenite catalyst which effects a preferential isomerization on the paraffin components to less waxy, high V.I. isoparaffins. The second stage may be operated at high pressure by cascading the first stage product into the second stage or at a lower pressure, typically from 1480 to 7000 kPa (200 to 1000 psig). The second stage catalyst is preferably a noble metal containing zeolite Beta catalyst which is treated with oxalic acid to give a low Alpha Value, typically below 10. The second stage is carried out at relatively low temperature, typically from 316 DEG to 343 DEG C (600 DEG to 650 DEG F) with a 343 DEG C+ (650 DEG F+) conversion in the range of 10 to 20 weight percent of the second stage feed but with high selectivity for isomerization of the paraffins.

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