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07/17/1994 01:28 3109875=:3J T'S TEC-I F4H t? <br /> TPS TECHNOLOGIES INC. <br /> FROCE55 FLOW DE _.QRIPTIN <br /> Petroleum contaminated soil is fed into the cold feed storage system via <br /> a loader. 'f his soil then empties from the bottom of the hopper onto a <br /> conveyor ;system that passes across a weighing system to track and <br /> record the ongoing tons of sail being fed to the plant. The soil next <br /> enters the rotary dryer drum in the opposite end from, the primary Hauck <br /> burner. As the drum rotates, the soil travels forward toward the burner <br /> as a function of the drum's angle with reference to level. The specially <br /> designed fl ghting within the internal diameter of the drum, moves the <br /> soil constardy forward. Heat transfer takes place from the primary <br /> burner as a function of soil moisture, drum rotation speed, drum angle <br /> and primary burner output, These variables are changed to meet the <br /> local area "_I=an soil" standards. <br /> Once the soi! comes to the end of the dryer drum, it is forced to exit into <br /> a mixing discharge pugmiil (soil conditioner) where it is injected with <br /> clean water This water controls the dust and allows the soil to become <br /> compactible again. Typical moisture contents end up around 10% - <br /> 15%. After exiting the pugmill, the dirt falls through a short vertical <br /> chute onto a conveyor where it is stacked up for sampling and removal <br /> for re-use. <br /> Since this system Is a counter flow heat exchanger, the gases and <br /> airborne dus: generated from the evaporation of the water and petroleum <br /> contaminatio-, in the soil, along with the ensuing dust created from the <br /> turbulent vetting, fiow out the opposite end of the dryer drum into a <br /> vertical cycl:,ne. Once in the cyclone, the large- dust particles are <br /> centrifuged out of the gas stream. These particles fall to the bottom of <br /> the cyclore where they are augered back into the discharge end of the <br /> dryer drun'i. Once in the drum, they are re-mixed with the cleaned dirt, <br /> heated bark up to the dart temperature and exit the drum with the dirt <br /> into the discharge pugmill. <br /> The water vapor, remaining dust particulate and volatile organic <br /> compounds !VOCs) pass out of the cyclone and into the oxidizer where <br /> the VOCs ora ompletely combusted at a minimum of 1450°F for 1 .5 <br /> seconds. <br />