Abstract: A method of mixing a crosslinking blend in a portable tote for use to crosslink polymer modified asphalts. The method includes providing a portable tote, where the tote includes a tank having a sidewall, a top and a bottom portion. Fixedly positioned partially within the tank interior is an air mixing system that includes a hollow wand that has a distal and a proximal end. The proximal end of the wand exits the tank. The distal end of the tote is connected to at least one accumulator plate, where the accumulator plate is adjacent to the interior bottom portion of the tank. Stored in the interior of the tank is a crosslinking blend suitable for use to crosslink polymer modified asphalts. The method includes the steps of attaching a pulsed gas controller to the proximal end of the wand and coupling a source of compressed gas to the controller, then activating the controller to cause mixing of the crosslinking blend by pulsing gases into the crosslinking blend for a sufficient period of time.

Abstract: A method of mixing a crosslinking blend in a portable tote for use to crosslink polymer modified asphalts. The method includes providing a portable tote, where the tote includes a tank having a sidewall, a top and a bottom portion. Fixedly positioned partially within the tank interior is an air mixing system that includes a hollow wand that has a distal and a proximal end. The proximal end of the wand exits the tank. The distal end of the tote is connected to at least one accumulator plate, where the accumulator plate is adjacent to the interior bottom portion of the tank. Stored in the interior of the tank is a crosslinking blend suitable for use to crosslink polymer modified asphalts. The method includes the steps of attaching a pulsed gas controller to the proximal end of the wand and coupling a source of compressed gas to the controller, then activating the controller to cause mixing of the crosslinking blend by pulsing gases into the crosslinking blend for a sufficient period of time.

Abstract: Production of propylene oxide by hydrolysis of propylene chlorohydrin in an aqueous alkaline reaction medium having a pH above 12 and a temperature of at least about 85.degree. C., is conducted in the presence of a small scale-inhibiting amount of a scale inhibitor added as a water-soluble polymer of acrylic acid having a weight average molecular weight in the range of about 1000 to about 5000, and in the absence of any phosphorus-containing additive component. A significant increase in acrylic polymer performance occurs under these high pH conditions as compared to performance at lower pH. Moreover, experiments have shown that no scale deposits were formed in a hydrolyzer unit operated for 180 days under conditions which normally require removal of deposits after 90 days of operation.