US 11,999,909 B2
Asphalt air blowing with liquid jet ejector and coil
Keith K. Aldous, Montgomery, TX (US); Sara K. Green, Houston, TX (US); William R. Harrison, Bushkill, PA (US); Vincent Kroll, Katy, TX (US); and Kevin Sutowski, Basking Ridge, NJ (US)
Assigned to EXXONMOBIL TECHNOLOGY AND ENGINEERING COMPANY, Annandale, NJ (US)
Filed by ExxonMobil Technology and Engineering Company, Annandale, NJ (US)
Filed on May 19, 2022, as Appl. No. 17/664,164.
Prior Publication US 2023/0374391 A1, Nov. 23, 2023
Int. Cl. C10C 3/04 (2006.01); B01F 25/312 (2022.01); B01J 10/00 (2006.01); B01J 19/24 (2006.01)
CPC C10C 3/04 (2013.01) [B01F 25/312 (2022.01); B01J 10/005 (2013.01); B01J 19/2465 (2013.01)] 15 Claims
OG exemplary drawing
 
1. A process for increasing the softening point of asphalt comprising the following steps:
providing an eductor comprising a motive inlet, a motive nozzle, a suction port, a main eductor body, a venturi throat and diffuser, and a discharge connection;
conducting a preheated asphalt feed including fresh asphalt and recycled oxidized asphalt, at a temperature from 150° C. to 300° C., as a motive liquid into the motive inlet of the eductor;
drawing an input gas containing oxygen into the suction port of the eductor;
mixing the preheated asphalt within the main eductor body with the input gas from the suction port of the eductor to form a gas/asphalt mixture;
conducting the gas/asphalt mixture to a heated and pressurized oxidizer vessel via piping connected to the discharge connection of the eductor, wherein the piping enables a bubble flow pattern to develop therein to enable reaction of the oxygen with the asphalt, the conducting comprising conducting the gas/asphalt mixture via the piping for a residence time of at least 5 seconds;
ejecting the oxygen entrained asphalt mixture from an exit port of the piping, wherein the exit port of the piping is within the oxidizer vessel; and
collecting off-gas from the overhead of the oxidizer vessel and an oxidized asphalt product stream from the bottom of the oxidizer vessel, and recycling a portion of the oxidized asphalt product stream back to the eductor to form the recycled oxidized asphalt; and
wherein the oxidized asphalt product stream has a softening temperature greater than the preheated asphalt feed.