The air is released to a dilute NCG system and the broken soap is further deaerated in a concentrator. Filtrate then stored in a weak
liquor tank will build up a soap layer through natural processes, which may be removed by manual skimming or continuous skimming.
Manual skimming requires the addition of nozzles up and down the side of the tank at different elevations to allow decanting of soap
at different levels. Continuous skimming utilizes a floating soap intake that rests on the soap-liquor interface. The use of swivel
joints in the soap outlet piping allows movement of the float with the change in liquor level.
Soap in black liquor is at its lowest solubility midway through an evaporator set. Here the soap is allowed to decant from the liquor
in a soap skim tank with a continuous rake mechanism skimming the soap from the top. The tank size may be reduced by adding air to the
liquor to improve the flotation of the soap. The level in the skim tank is maintained by the use of an external adjustable weir standpipe.
Depending upon the care taken in a number of the recovery steps above, the separated soap may contain a large amount of black liquor.
The black liquor not only costs money to ship to the tall oil processing plant but also represents a handling issue at the tall oil processing
plant. Black liquor can affect the equipment used to separate the acidulated soap from the brine as well as increase the TRS emissions from
the plant. A Lundberg Associates' soap separator is designed to remove at least 50% of the liquor from the soap. The mechanism utilizes
rotating tines to provide a path for the lower viscosity liquor to separate from the soap.