The entire scope of the project included construction of a new island that would be home to a six-effect, falling film evaporator train that would produce 74% product solids at an evaporation rate of 897k lbs/hr (407 T/h). The system would also process precipitator slurry, tall-oil brine, and other recovered boilout liquor streams.
Two major components of the process equipment were instrumental in achieving the objectives for the mill. These included:
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Enhanced forced circulation technology which enables turbulence of the black liquor at high viscosities with lower recirculation rates, thus requiring less horsepower than conventional forced circulation.
This allows mixing of the bulk product solids that results in increased heat transfer efficiency to minimize the laminar layer on the tube wall surface to greatly reduce fouling in the heater to achieve higher solids concentration.
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Analysis of the precipitator slurry revealed high levels of chloride. If left untreated, unfavorable conditions could develop such as plugging of the super heater, corrosion in the recovery boiler and increased steam demand.
The CRP (Chloride Removal Process) system removes non-process elements such as chloride and potassium from the chemical makeup that accumulate in the recovery cycle. Removal of these elements via the CRP, rather than purging the raw precipitator ash, reduces the amount of purge to achieve the same results.
Other equipment supplied to the evaporator island included a salt cake crystallizer, a soap skimming tank, cooling towers and chemical building, a foul condensate tank, a new MCC facility and control system. Outside of the island, a new indirect black liquor heater system was installed.