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baths, energy must only be added to make up for that which is lost through convection and radiation. The glue is required to be maintained at a temperature of 285°F to prevent it from solidifying. With this as the internal temperature, the outside surface temperatures can be calculated. The outside surface temperature of three of the four outside surfaces is estimated to be the same temperature which can be found to be 83°F. The surface temperature for the remaining side which includes the heat exchanger operating at a temperature of 285°F located in the space between the tank and the insulation to supply the energy into the glue bath is found to be 95°. The outer surface temperature of the insulation was calculated using a computer software program published by the North American Insulation Manufacturers Association (NAIMA) called 3E Plus [46] which is also able to calculate the heat loss and the surface temperature of different types of surfaces and uses a database of many different types of insulation. This calculation takes into account both convection and radiation heat losses from the surface. To more accurately predict the heat loss and in turn the amount of heat addition required, the tank was broken as previously described with three of the four outer sides having an interior surface temperature of 175°F. The one side containing the waste heat energy addition heat exchanger’s surface temperature was fixed to the supply temperature of 285°F and the top is assumed to be open to the atmosphere. These operating temperatures were used to calculate the outer surface temperature and heat loss. The following calculation shows the total surface areas and the total amount of heat energy that must be added to the glue baths to maintain the temperature. 93PDF Image | TUDY OF LOW-GRADE WASTE HEAT RECOVERY
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