Patent classifications
F02B51/02
Split cycle engine
A split cycle internal combustion engine includes a combustion cylinder accommodating a combustion piston and a compression cylinder accommodating a compression piston. The engine also includes a controller arranged to receive an indication of a parameter associated with the combustion cylinder and/or a fluid associated therewith and to control an exhaust valve of the combustion cylinder in dependence on the indicated parameter to cause the exhaust valve to close during the return stroke of the combustion piston, before the combustion piston has reached its top dead centre position (TDC), when the indicated parameter is less than a target value for the parameter; and close on completion of the return stroke of the combustion piston, as the combustion piston reaches its top dead centre position (TDC), when the indicated parameter is equal to or greater than the target value for the parameter.
POWER GENERATION SYSTEMS AND METHODS REGARDING SAME
An electrochemical power system is provided that generates an electromotive force (EMF) from the catalytic reaction of hydrogen to lower energy (hydrino) states providing direct conversion of the energy released from the hydrino reaction into electricity, the system comprising at least two components chosen from: H.sub.2O catalyst or a source of H.sub.2O catalyst; atomic hydrogen or a source of atomic hydrogen; reactants to form the H.sub.2O catalyst or source of H.sub.2O catalyst and atomic hydrogen or source of atomic hydrogen; and one or more reactants to initiate the catalysis of atomic hydrogen. The electrochemical power system for forming hydrinos and electricity can further comprise a cathode, an anode, reactants that constitute hydrino reactants during cell operation with separate electron flow and ion mass transport, a source of oxygen, and a source of hydrogen. Due to oxidation-reduction electrode reactions, the hydrino-producing reaction mixture is constituted with the migration of electrons through an external circuit and ion mass transport through a separate path such as the electrolyte to complete an electrical circuit. In an embodiment, the anode is regenerated by intermittent charging with the electrodeposition of the anode metal ion from the electrolyte to the anode wherein an anion exchange with the anode metal oxide provides a thermodynamically favorable cycle to facilitate the electrodeposition.
A solid fuel power source that provides at least one of thermal and electrical power such as direct electricity or thermal to electricity is further provided that powers a power system comprising (i) at least one reaction cell for the catalysis of atomic hydrogen to form hydrinos, (ii) a chemical fuel mixture comprising at least two components chosen from: a source of H.sub.2O catalyst or H.sub.2O catalyst; a source of atomic hydrogen or atomic hydrogen; reactants to form the source of H.sub.2O catalyst or H.sub.2O catalyst and a source of atomic hydrogen or atomic hydrogen; one or more reactants to initiate the catalysis of atomic hydrogen; and a material to cause the solid fuel to be highly conductive, (iii) at least one set of electrodes that confine the fuel and an electrical power source that provides a short burst of low-voltage, high-current electrical energy to initiate rapid kinetics of the hydrino reaction and an energy gain due to forming hydrinos, (iv) a product recovery systems such as a condensor, (v) a reloading system, (vi) at least one of hydration, thermal, chemical, and electrochemical systems to regenerate the fuel from the reaction products, (vii) a heat sink that accepts the heat from the power-producing reactions, (vi
POWER GENERATION SYSTEMS AND METHODS REGARDING SAME
An electrochemical power system is provided that generates an electromotive force (EMF) from the catalytic reaction of hydrogen to lower energy (hydrino) states providing direct conversion of the energy released from the hydrino reaction into electricity, the system comprising at least two components chosen from: H.sub.2O catalyst or a source of H.sub.2O catalyst; atomic hydrogen or a source of atomic hydrogen; reactants to form the H.sub.2O catalyst or source of H.sub.2O catalyst and atomic hydrogen or source of atomic hydrogen; and one or more reactants to initiate the catalysis of atomic hydrogen. The electrochemical power system for forming hydrinos and electricity can further comprise a cathode, an anode, reactants that constitute hydrino reactants during cell operation with separate electron flow and ion mass transport, a source of oxygen, and a source of hydrogen. Due to oxidation-reduction electrode reactions, the hydrino-producing reaction mixture is constituted with the migration of electrons through an external circuit and ion mass transport through a separate path such as the electrolyte to complete an electrical circuit. In an embodiment, the anode is regenerated by intermittent charging with the electrodeposition of the anode metal ion from the electrolyte to the anode wherein an anion exchange with the anode metal oxide provides a thermodynamically favorable cycle to facilitate the electrodeposition.
A solid fuel power source that provides at least one of thermal and electrical power such as direct electricity or thermal to electricity is further provided that powers a power system comprising (i) at least one reaction cell for the catalysis of atomic hydrogen to form hydrinos, (ii) a chemical fuel mixture comprising at least two components chosen from: a source of H.sub.2O catalyst or H.sub.2O catalyst; a source of atomic hydrogen or atomic hydrogen; reactants to form the source of H.sub.2O catalyst or H.sub.2O catalyst and a source of atomic hydrogen or atomic hydrogen; one or more reactants to initiate the catalysis of atomic hydrogen; and a material to cause the solid fuel to be highly conductive, (iii) at least one set of electrodes that confine the fuel and an electrical power source that provides a short burst of low-voltage, high-current electrical energy to initiate rapid kinetics of the hydrino reaction and an energy gain due to forming hydrinos, (iv) a product recovery systems such as a condensor, (v) a reloading system, (vi) at least one of hydration, thermal, chemical, and electrochemical systems to regenerate the fuel from the reaction products, (vii) a heat sink that accepts the heat from the power-producing reactions, (vi
DEVICE HAVING AN ACTIVE COATING COMPRISING NANO CATALYST OF OXIDES OF TITANIUM, SILICON AND ALUMINUM FOR SAVING FUEL IN A COMBUSTION CHAMBER
The present invention relates to a fuel saving device for a combustion chamber comprising a coating on a surface in fuel passageway of the device through which the fuel to be entered and burnt in the combustion chamber flows, wherein the coating comprises nanosized particles of TiO.sub.2, SiO.sub.2 and Al.sub.2O.sub.3 in an epoxy coating composition.
DEVICE HAVING AN ACTIVE COATING COMPRISING NANO CATALYST OF OXIDES OF TITANIUM, SILICON AND ALUMINUM FOR SAVING FUEL IN A COMBUSTION CHAMBER
The present invention relates to a fuel saving device for a combustion chamber comprising a coating on a surface in fuel passageway of the device through which the fuel to be entered and burnt in the combustion chamber flows, wherein the coating comprises nanosized particles of TiO.sub.2, SiO.sub.2 and Al.sub.2O.sub.3 in an epoxy coating composition.
MARINE METHANOL INERT GAS BLANKETING
An inert blanket system includes a reformer that produces hydrogen gas and carbon dioxide. The hydrogen gas is separated from the carbon dioxide. The carbon dioxide is ported to a vapor region of a tank to reduce the flammability of the gases in the vapor region of the tank. Excess carbon dioxide is ported to an overflow system designed to store the excess carbon dioxide for future use or to sequester the carbon dioxide.
MARINE METHANOL INERT GAS BLANKETING
An inert blanket system includes a reformer that produces hydrogen gas and carbon dioxide. The hydrogen gas is separated from the carbon dioxide. The carbon dioxide is ported to a vapor region of a tank to reduce the flammability of the gases in the vapor region of the tank. Excess carbon dioxide is ported to an overflow system designed to store the excess carbon dioxide for future use or to sequester the carbon dioxide.
Control device for internal combustion engine and control method for internal combustion engine
An internal combustion engine in which when the gas temperature of a fuel reformation chamber when a piston in a fuel reformation cylinder reaches the compression top dead point is estimated to be equal to or higher than a soot generation lower limit temperature set according to an equivalence ratio of the fuel reformation chamber, a reaction gas temperature adjusting operation for suppressing or reducing an increase in the reaction gas temperature in the fuel reformation chamber is executed. Further, a closing timing of an air-intake valve is changed to reduce an effective compression ratio of the fuel reformation chamber.
Control device for internal combustion engine and control method for internal combustion engine
An internal combustion engine in which when the gas temperature of a fuel reformation chamber when a piston in a fuel reformation cylinder reaches the compression top dead point is estimated to be equal to or higher than a soot generation lower limit temperature set according to an equivalence ratio of the fuel reformation chamber, a reaction gas temperature adjusting operation for suppressing or reducing an increase in the reaction gas temperature in the fuel reformation chamber is executed. Further, a closing timing of an air-intake valve is changed to reduce an effective compression ratio of the fuel reformation chamber.
Control device for internal combustion engine and control method for internal combustion engine
An internal combustion engine in which a required reformed-fuel heat generation quantity (required output cylinder heat generation quantity) is calculated based on a required engine power and the thermal efficiency of an output cylinder. An estimated reformed fuel heat generation quantity is calculated based on the molar number of reformed fuel, mole fraction of each gas component in the reformed fuel, and heat generation quantity of each gas component in the reformed fuel. When a value resulting from subtracting the estimated reformed fuel heat generation quantity from the required reformed-fuel heat generation quantity is negative, a fuel reforming operation is not executed, assuming that there is a possibility that surplus reformed fuel may be generated. For example, a fuel supply from an injector to a fuel reformation chamber is stopped.