Apparatuses for gasifying glycerol using solar energy, system including the apparatuses, and methods of using the apparatuses are provided. The apparatuses may include a concentrated solar dish comprising an opening and a gasifying reactor comprising a chamber. An entrance of the chamber may be aligned to the opening. The apparatuses may also include a thermal insulator disposed on outer surfaces of the concentrated solar dish and the gasifying reactor and a pipe in the thermal insulator. The pipe may be configured to deliver glycerol into the chamber of the gasifying reactor in the form of atomized mist. The glycerol may be delivered to a portion of the chamber adjacent the opening.

The invention provides particulate compositions, which generate hydrogen when contacted with water, the compositions comprising particles of: aluminium; one or more metal oxides; and one or more chloride salts of alkali metals or alkaline earth metals.

The invention also provides methods of preparing such compositions and methods of generating hydrogen by contacting the compositions with water.

A zero emission waste system comprising a waste treatment unit that couples to a facility. The waste treatment unit is onsite with the facility either within the facility or local to the facility for treating waste produced by the facility. Alternatively, the waste treatment unit can be mobile that is designed to couple to the facility for waste disposal. The waste treatment unit comprises a gasification reactor, a syngas treatment unit, and a synthetic fuel generator for treating and converting waste. The synthetic fuel generator comprises an electrolysis unit and a liquid fuel synthesis unit. The waste treatment unit converts the waste to synthetic fuel, gaseous fuel, oxygen, heat, slag, and other components that are useful to the facility or other entities. The waste treatment system uses carbon dioxide generated during a waste conversion process thereby producing substantially zero emissions and eliminating waste that could be harmful to the environment.

A zero emission waste system comprising a waste treatment unit that couples to a facility. The waste treatment unit is onsite with the facility either within the facility or local to the facility for treating waste produced by the facility. Alternatively, the waste treatment unit can be mobile that is designed to couple to the facility for waste disposal. The waste treatment unit comprises a gasification reactor, a syngas treatment unit, and a synthetic fuel generator for treating and converting waste. The synthetic fuel generator comprises an electrolysis unit and a liquid fuel synthesis unit. The waste treatment unit converts the waste to synthetic fuel, gaseous fuel, oxygen, heat, slag, and other components that are useful to the facility or other entities. The waste treatment system uses carbon dioxide generated during a waste conversion process thereby producing substantially zero emissions and eliminating waste that could be harmful to the environment.

This invention provides a reversible hydrogen loading and discharging system and a reversible method for loading and discharging hydrogen. The system and the methods of this invention comprise ethylene glycol as a liquid organic hydrogen carrier and at least one transition metal. By reacting ethylene glycol with at least one transition metal; at least one hydrogen molecule and at least one oligoester of ethylene glycol are formed (hydrogen releasing)⋅, and by reacting at least one oligoester of ethylene glycol with at least one transition metal and at least one hydrogen molecule, at least one ethylene glycol is formed (hydrogen loading).

The invention is directed to a co-gasification process that uses biomass and VGO as a feedstock to produce syngas which includes a mixture of carbon monoxide and hydrogen.

The present disclosure refers in one embodiment to processes for making and transporting clean hydrogen fuel. The processes may involve hydrotreating, hydrocracking, or both hydrotreating and hydrocracking an aromatic feedstock under conditions to obtain a liquid hydrocarbon fuel. The liquid hydrocarbon fuel is hydrogenated to obtain a hydrogen-rich fuel that is transported to a dehydrogenation facility that may also be at or near a hydrogen station. The hydrogen-rich fuel is used to obtain hydrogen and a second liquid hydrocarbon fuel.

The present disclosure relates generally to a carbon-neutral process for the generation of carbon-neutral hydrogen and carbon-neutral electricity. More specifically, the present disclosure relates to compositions, methods and apparatus employing a carbon-neutral process for generating electricity employing a liquid organic hydrogen carrier (LOHC) for supplying hydrogen for generating the carbon neutral electricity. The present disclosure also relates more specifically to carbon-neutral compositions consisting of liquid organic hydrogen carriers used for supplying hydrogen to generate electricity that may be regenerated in a carbon-neutral process using an apparatus with a net zero atmospheric emission of carbon oxides.

A process for dehydrogenating organic molecules (OM) and a reaction vessel (RB) suitable for the process for dehydrogenating organic molecules by means of an inductive field (IF), wherein the reaction vessel comprises a device for generating an inductive field and a solid loose material (FLM), and wherein the reaction vessel and its contents are free of platinum, palladium, rhodium, gold, iridium, titanium, tantalum or ruthenium.

A dihydrogen generator (5) comprising a chamber (10), a reservoir (260) for containing a reagent and a catalytic system (15), the chamber being impervious to dihydrogen and defining an internal chamber space (45), the reservoir being housed in the internal chamber space and comprising a reservoir wall (270, 275) impervious to a liquid and permeable to dihydrogen, the catalytic system being disposed at least partly in the reservoir and comprising a catalyst (205) for the reaction that generates dihydrogen from the reagent, the chamber comprising a discharge valve (300) for withdrawing the dihydrogen from the internal chamber space, an injection valve (295) for injecting the liquid into the reservoir and a drain valve (460) for draining the liquid from the reservoir.