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Slurry Tank Heating

Overview

Steam sparging nozzles for slurry tank heating in ethanol plants may be the current industry standard but also has its disadvantages. High steam temperatures (up to 350°F) can damage starch and enzymes, uneven heat distribution from bottom-only steam injection leaves enzymes at suboptimal conditions, poor steam mixing causes cavitation, and uncondensed steam escapes, wasting energy and increasing costs.
Direct Steam Injection (DSI) heaters offer a highly effective slurry tank solution over sparging:
  • Ensures higher quality starch conversion by preventing hot spots, optimizing enzyme utilization, and achieving consistent discharge temperature
  • Maintains accurate temperature control, minimizing variations across the tank for optimized enzyme retention and starch conversion
  • Reduces maintenance by containing steam injection externally, preventing damage to the slurry tank and spargers
  • Saves energy by condensing all steam if used in the Hydroheater, minimizing steam loss and lowering boiler fuel usage
  • Facilitates particle size reduction through added shear that breaks up “dough bars” and exposes more starch surface area and improving starch conversion