An apparatus for the production of hydrogen peroxide. The apparatus can have a substrate consisting of a substantially triboelectrically neutral material, a catalyst disposed upon the substrate, and an energy source to provide energy for ambient oxygen and water vapor to react and form hydrogen peroxide. The apparatus does not produce any ozone as a byproduct. The apparatus produces pure hydrogen peroxide gas which is not insulated by water molecules. Further the hydrogen peroxide gas, due to the fact that it is uninsulated by water molecules, is self-regulating to a concentration of 0.03 parts per million even when continuously produced by the apparatus.

An apparatus for the production of hydrogen peroxide. The apparatus can have a substrate consisting of a substantially triboelectrically neutral material, a catalyst disposed upon the substrate, and an energy source to provide energy for ambient oxygen and water vapor to react and form hydrogen peroxide. The apparatus does not produce any ozone as a byproduct. The apparatus produces pure hydrogen peroxide gas which is not insulated by water molecules. Further the hydrogen peroxide gas, due to the fact that it is uninsulated by water molecules, is self-regulating to a concentration of 0.03 parts per million even when continuously produced by the apparatus.

A fuel-saving device includes an oxygen generator adapted for producing oxygen, an air intake component adapted for inhaling air, and a conveyor comprising an output terminal adapted for outputting gas, an oxygen terminal connected with the oxygen generator, an air terminal connected with the air intake component, and a connector connecting the output terminal, the oxygen terminal and the air terminal, so as to allow oxygen from the oxygen generator and air from the air intake component to be mixed and output through the output terminal.

A fuel-saving device includes an oxygen generator adapted for producing oxygen, an air intake component adapted for inhaling air, and a conveyor comprising an output terminal adapted for outputting gas, an oxygen terminal connected with the oxygen generator, an air terminal connected with the air intake component, and a connector connecting the output terminal, the oxygen terminal and the air terminal, so as to allow oxygen from the oxygen generator and air from the air intake component to be mixed and output through the output terminal.

A method of using magnetic influence on flow streams of liquids and gases to over excite their atoms, break existing molecular bonds, and from two oppositely charged flow streams cause immediate and permanent bonding of oppositely charged ions to create a new molecular composition. While magnetic influence is predominately responsible for the molecular reorganization produced, induced turbulence disrupts a tendency for laminar flow in the flow streams, creating more chaotic movement and molecule collisions in liquids/gases used and a more complete result. Mixing of the two oppositely charged flow streams is preferred via a venturi. Magnetic influence on flow streams can be applied more than once. Using this method with water having a molecular composition of H.sub.2O in a primary flow stream and ozone gas in a secondary flow stream, and mixing of the oppositely charged flow streams using a venturi, a new molecular composition of H.sub.2O.sub.5 can be created.

A thermal and non-thermal plasma activated water reactor system is provided that includes a reaction chamber, where the reaction chamber includes a gas inlet, a water inlet, a gas and water outlet, a ground electrode and reaction electrodes, where the water inlet and the water outlet are disposed to form a water vortex in the reaction chamber when water flows there through, where the reaction electrodes include a thermal plasma electrode and a non-thermal plasma electrode, and a plasma activated water reservoir that is disposed to receive the plasma activated water from the reaction chamber and disposed to return the plasma activated water to the reaction chamber.

A thermal and non-thermal plasma activated water reactor system is provided that includes a reaction chamber, where the reaction chamber includes a gas inlet, a water inlet, a gas and water outlet, a ground electrode and reaction electrodes, where the water inlet and the water outlet are disposed to form a water vortex in the reaction chamber when water flows there through, where the reaction electrodes include a thermal plasma electrode and a non-thermal plasma electrode, and a plasma activated water reservoir that is disposed to receive the plasma activated water from the reaction chamber and disposed to return the plasma activated water to the reaction chamber.

The electrochemical reactors disclosed herein provide novel oxidation and reduction chemistries and employ in-creased mass transport rates of materials to and from the surfaces of electrodes

The electrochemical reactors disclosed herein provide novel oxidation and reduction chemistries and employ in-creased mass transport rates of materials to and from the surfaces of electrodes

The electrochemical reactors disclosed herein provide novel oxidation and reduction chemistries and employ increased mass transport rates of materials to and from the surfaces of electrodes therein.