Other

Florida Power Corporation

Florida Progress Corporation

Antonio A Padilla

Ned B Spake

Larry A Rodriguez

Robert A Ashworth

W Wes Berry

Warnie L Sage

Rae A Schmeda

F Dave Sanderlin

Fred S Gunnerson

Joy R Iurato

A system of sealed heat pipes enclosing a working fluid. In the heating mode, the working fluid is evaporated and the latent heat of vaporization is transported through the heat pipes to the condenser region. The condensate returns to the evaporator region through a liquid bypass line containing a liquid storage reservoir and a heating control valve. In the cooling mode, a cooling control valve is opened to increase the specific volume of the heat pipe system. During operation, heat is absorbed from the evaporator region and transferred by the working fluid vapor through the heat pipe system to the cold media. Condensate returns to the external evaporator by a liquid return line containing a liquid storage reservoir and a cooling control valve. Electric resistance heating can be incorporated to heat the reservoir. Vapor from the reservoir passes into the heat pipe system through a check valve vapor line. Shutdown and system control are regulated by the reservoir cutoff valve and electric heating.

Controllable heat pipes for thermal energy transfer

The method of the present invention is a novel comprehensive process for maximizing the recovery of valuable mineral values from coal ash. Options may also be included for the production of saleable inorganic chemical by-products. The process employs both physical and chemical extraction techniques that maximize the yield of products while reducing the quantity of waste produced. Valuable minerals and chemicals such as cenospheres (hollow microspheres), carbon, magnetite (Fe.sub.3 O.sub.4), alumina (Al.sub.2 O.sub.3), iron oxide (Fe.sub.2 O.sub.3) and iron chloride (FeCl.sub.3) may be produced. Due to removal of carbon, magnetite, and iron oxide from the coal ash, the processed ash comprises a quality pozzolan.

Method for the recovery of minerals and production of by-products from

Large power transformers such as used at electrical generating plants utilize oil for cooling with the heat removed by air cooled radiators. Several air cooled radiators are removed from the transformers and the oil circulated through plate heat exchangers which provide a heat transfer path to a fluid cooling medium such as water. Flow transducers and electrical temperature sensors may be used to monitor the flow rates of the oil and water, and the temperature of the oil and water in various parts of the system. These parameters are controlled to maximize the transfer of waste heat from the transformer to the water. The heated water is then utilized to perform useful work. For example, in a power plant having package boilers, the boiler makeup water is preheated with the transformer waste heat thereby reducing the energy requirements of the system.

Power transformer waste heat recovery system

A method for desulfurization, denitrification, and oxidation, of carbonaceous fuels including a two stage oxidation technique. The carbonaceous fuel, containing ash, along with an oxygen-containing gas is introduced into a first stage partial oxidation unit containing a molten ash slag maintained at a temperature of about 2200.degree.-2600.degree. F. A flux may also be introduced into the first stage partial oxidation unit for the purpose of increasing the basicity and maintaining the viscosity of the molten ash slag at a value no greater than about 10 poise. The carbonaceous fuel is gasified, and sulfur is chemically bound and captured in the molten ash slag. Since the first stage is operated in a gasification mode (reducing atmosphere), essentially all of the nitrogen in the fuel is converted to diatomic nitrogen, which results in low nitrogen oxide emissions upon final combustion. The first stage is also designed to physically remove a major portion of the fuel ash, the ash leaving the system as a molten slag. The combustible gas derived from partial oxidation (gasification) is directed along a substantially horizontal path to a second stage oxidation unit for final combustion. The sulfur-containing molten slag is removed to a water-sealed quench system or indirect water cooled system for disposal.

Method for desulfurization, denitrifaction, and oxidation of

An improved fuel composition is provided comprising in minor proportion a non-dewatered sewage sludge and in major proportion a particulate solid fuel. A method is also provided for the incineration of sewage sludge comprising providing a pumpable admixture of a non-dewatered sewage sludge and a particulate solid fuel and incinerating the admixture.

Alternative fuel comprised of sewage sludge and a particulate solid fuel

A method for desulfurization and oxidation of carbonaceous fuels including a two stage oxidation technique. The carbonaceous fuel, along with an oxygen-containing gas is introduced into a first stage partial oxidation unit containing molten slag maintained at a temperature of about 2200.degree.-2600.degree. F. A flux may also be introduced into the first stage partial oxidation unit for the purpose of maintaining the viscosity of the molten slag at a value no greater than about 10 poise. The carbonaceous fuel is gasified, and sulfur is chemically bound and captured in the molten slag. The combustible gas derived from partial oxidation and gasification is directed along a substantially horizontal path to a second stage oxidation unit for final combustion. The sulfur-containing slag is removed to a water-sealed quench system for disposal.

Growing community of inventors

Tampa, FL, United States of America

Antonio A Padilla