Abstract: A process is disclosed for the in situ conversion and recovery of heavy crude oils and natural bitumens from subsurface formations using either a continuous operation with one or more injection and production boreholes, which may include horizontal boreholes, or a cyclic operation whereby both injection and production occur in the same boreholes. A mixture of reducing gases, oxidizing gases, and steam are fed to downhole combustion devices located in the injection boreholes. Combustion of the reducing gas-oxidizing gas mixture is carried out to produce superheated steam and hot reducing gases for injection into the formation to convert and upgrade the heavy crude or bitumen into lighter hydrocarbons. Communication between the injection and production boreholes in the continuous operation and fluid mobility within the formation in the cyclic operation is induced by fracturing or related methods.

Abstract: An integrated process is disclosed for treating, at the surface, production fluids recovered from the application of in situ hydrovisbreaking to heavy crude oils and natural bitumens deposited in subsurface formations. The production fluids include virgin heavy hydrocarbons, heavy hydrocarbons converted via the hydrovisbreaking process to lighter liquid hydrocarbons, residual reducing gases, hydrocarbon gases, and other components. In the process of this invention, the hydrocarbons in the production fluids are separated into a synthetic-crude-oil product (a nominal butane to 975.degree. F. fraction with reduced sulfur, nitrogen, metals, and carbon residue) and a residuum stream (a nominal 975.degree. F.+ fraction). Partial oxidation of the residuum is carried out to produce clean reducing gas and fuel gas for steam generation, with the reducing gas and steam used in the in situ hydrovisbreaking process.

Abstract: A method and apparatus for reducing particle emissions from combustion processes and increasing combustion efficiency. A high voltage electrical potential is passed through a combustion flame to agglomerate particles, which are then removed from the exhaust gases through combustion or deposition on nearby surfaces of the apparatus. It is believed that application of high voltage electrical potential increases movement of the ions and free electrons within the combustion flame, causing increased oxygen mixing, and combustion efficiency. In one embodiment of the invention, a high voltage electrical potential is applied to the combustion flames of a wood stove and secondary air is supplied in the vicinity of the upper periphery of the flames. Application of the high voltage electrical potential and secondary air dramatically reduces particle emissions produced by the wood stove.

Abstract: A system and method provides for burning wood particles or other combustible fibrous particles at a continuous high rate in which the particles are at least partially pyrolyzed as they are being fed into a combustion chamber, complete combustion of the particles and pyrolysis products occuring within the combustion chamber. Pyrolysis is enabled by mixing the particles with air having a temperature of at least 600.degree. F. The system enables the burning of green wood in existing large boiler systems as well as in gas turbine systems; the latter operatable with a high pressure combustion chamber. In a boiler system, air for pyrolysis of the particles may be heated by the boiler, in a turbine system, air for pyrolysis of the particles may be heated by a compressor driven by a turbine.

Abstract: A polyphase composition for the storage of heat or cold utilizing the latent heat of fusion of a salt hydrate continuous phase intimately intermixed with a hydrated hydraulic cement continuous phase and wherein said continuous phases are optionally in contact with a discontinuous crystalline phase comprising a nucleating component and wherein the composition is enveloped, contained, or packaged within a vapor impermeable material.

Abstract: In a fuel gas distribution system, at least one fuel gas stream is mixed with air to achieve a heating value equivalency which is the same as that of another fuel gas having a different heating value and specific gravity. The heating value equivalency is defined as the heating value of a fuel gas in heat units per unit of volume divided by the square root of the specific gravity of the gas. A control system is employed to measure the specific gravity, pressure, temperature and flow rate of the first gas in a first gas stream, and the pressure, temperature and flow rate of air in a second stream, and to control the flow rate of the gas from the first stream and air from the second stream such that the resulting mixture from the two streams has the same heating value equivalency as that of a third gas which was used to adjust the gas burners for use in that system.

Abstract: A horizontal water filled vaporizer chamber is heated through the instrumentality of a horizontal combustion chamber extending through a lower portion of the vaporizer chamber. A first plenum inside the vaporizer chamber at a first end thereof receives combustion products from the chamber, and horizontal flues open to this first plenum carry these combustion products from it through the vaporizer chamber to a second plenum outside of the boiler where they are discharged up a stack. A plurality of vaporizer coils, each consisting of vertically spaced horizontal runs of pipe, extend from end to end in an upper portion of the vaporizer chamber. Each pair of adjacent pipe runs in each coil lie in a plane forming an acute angle with respect to a horizontal plane. Every vaporizer coil is connected inside the vaporizer chamber at its lower end to a liquid propane inlet header and at its upper end to a gaseous propane outlet header.

Abstract: A water bath vaporizer for converting liquid propane into gaseous propane includes a propane-carrying heat transfer pipe in the form of a helix immersed in a water bath in an insulated upright cylindrical water chamber. Multiple straight vertical flues are integral with a bottom plate and a top plate of the water chamber and are open through the water bath and the center of the helix to carry combustion products and heated air from a combustion chamber to a stack above. Liquid propane is introduced at the top of the helix and gaseous propane is removed from the bottom and is discharged vertically upwardly through a liquid cut-off float valve which prevents flow of liquid propane out of the vaporizer. A breather attachment includes a breather pipe having a first section extending outwardly from a top portion of the water chamber at a slight upward angle and having a vertical second section terminating in an upwardly opening outer end.