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(3.1) It can be seen from the above equation that in order for the acetone to be completely burned in air four parts of air are needed for one part of fuel. Since the average fuel flow rate is about 37 lbms of acetone per minute, the theoretical air flow rate is about 84,072 lbms/hr. Note that this is the average mass flow rate of air for stoichiometric conditions (complete combustion) and that the kiln is really going to be firing with more excess air in order to ensure that acetone is completely oxidized and to keep the operating temperature down. Since the ORC’s input heat needs to be a maximum of 200 degrees Fahrenheit the amount of heat being transferred from the baghouse to the ORC input can be calculated from the simple heat transfer equation shown below. 0 (3.2) Where Q is the amount of heat transferred from the baghouse to the ORC, Cp is the specific heat of air at the average temperature, mdot is the average mass flow rate of air through the kilns, Tbaghouse is 365 degrees Fahrenheit, and TORC is 200 degrees Fahrenheit. This will give the maximum heat transfer rate since the temperature difference is maximized but will be evaluated at the theoretical minimum mass flow rate of air. The maximum heat transfer was then determined to be about 3.8 MMBTU/hr for one kiln. Since the facility had two rotary kilns next to each other that were designed to be fired simultaneously the exhaust air could be ducted together to double the mass flow rate of air and ultimately double the rate of heat transferred from the exhaust to the ORC. 62PDF Image | NESTER, RYAN TIMOTHY. Organic Rankine Cycles: A Comparative Study and Analysis of Multiple Applications.
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