The present invention relates to a drinking product of vitamin D-fortified mineral water. The present invention further relates to methods of preparing packaged drinking product of the vitamin D-fortified water with minerals and/or natural mineral water, wherein the method essentially comprises water treatment, re-mineralization, ozonation, vitamin D dosing, and mineralization.

The present invention describes a processes, systems, and catalysts for the utilization of carbon dioxide into high quality synthesis gas that can then be used to produce fuels (e.g., diesel fuel) and chemicals. In one aspect, the present invention provides a process for the conversion of a feed gas comprising carbon dioxide and hydrogen to a product gas comprising carbon monoxide and water.

The present invention describes a processes, systems, and catalysts for the utilization of carbon dioxide into high quality synthesis gas that can then be used to produce fuels (e.g., diesel fuel) and chemicals. In one aspect, the present invention provides a process for the conversion of a feed gas comprising carbon dioxide and hydrogen to a product gas comprising carbon monoxide and water.

A method for irrigation of a crop capable of producing Cannabidiol (CBD) comprises irrigating the crop with a nanobubble hydrogen rich water (HRW-nano), whereby a concentration of CBD in the crop increased as a result of irrigating with the HRW-nano, compared to irrigation with an irrigation water having the same composition except without added hydrogen (control irrigation).

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800° F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800° F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst.

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800° F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800° F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst.

A method for generating a structurally altered gas molecule from water. An example method includes placing an electrolyte solution in a chemical reaction chamber, adding purified water to the chemical reaction chamber, and applying a focused magnetic field and an electric field to a mixture of the purified water and the electrolyte solution to cause generation of the structurally altered gas molecule from the purified water. The structurally altered gas molecule is a combination of two parts of hydrogen and one part of oxygen. The structurally altered gas molecule has a hydrogen-oxygen-hydrogen bond angle between 94 degrees and 104 degrees and hydrogen-oxygen bond length between 0.95 Angstrom and 1.3 Angstrom. The structurally altered gas molecule is stable at a pressure exceeding 300 pounds per square inch gauge.

A method for generating a structurally altered gas molecule from water. An example method includes placing an electrolyte solution in a chemical reaction chamber, adding purified water to the chemical reaction chamber, and applying a focused magnetic field and an electric field to a mixture of the purified water and the electrolyte solution to cause generation of the structurally altered gas molecule from the purified water. The structurally altered gas molecule is a combination of two parts of hydrogen and one part of oxygen. The structurally altered gas molecule has a hydrogen-oxygen-hydrogen bond angle between 94 degrees and 104 degrees and hydrogen-oxygen bond length between 0.95 Angstrom and 1.3 Angstrom. The structurally altered gas molecule is stable at a pressure exceeding 300 pounds per square inch gauge.

A process of producing potable water, by combining a hydrocarbon containing fossil fuel with oxygen, in a combustion device, such as a home heating or utility unit to produce a flue gas of water vapor and carbon dioxide, and condensing the water vapor in the flue gas to yield potable water. The combustion device can produce heat or electricity. The water vapor can be condensed with one or more heat exchange devices. The source of oxygen can be air, pure oxygen, or nitrogen reduced air. The source of oxygen can be humidified, such as with a non-potable water source or non-potable water can be added to the flue gas. The carbon dioxide and/or nitrogen in the flue gas can be reduced or removed before the condensation step(s). The pressure of the flue gas can be increased prior to condensation of the water vapor. Natural gas is a preferred fuel.

A process of producing potable water, by combining a hydrocarbon containing fossil fuel with oxygen, in a combustion device, such as a home heating or utility unit to produce a flue gas of water vapor and carbon dioxide, and condensing the water vapor in the flue gas to yield potable water. The combustion device can produce heat or electricity. The water vapor can be condensed with one or more heat exchange devices. The source of oxygen can be air, pure oxygen, or nitrogen reduced air. The source of oxygen can be humidified, such as with a non-potable water source or non-potable water can be added to the flue gas. The carbon dioxide and/or nitrogen in the flue gas can be reduced or removed before the condensation step(s). The pressure of the flue gas can be increased prior to condensation of the water vapor. Natural gas is a preferred fuel.