Patent classifications
C01B3/061
SYSTEMS AND METHODS FOR GENERATING HYDROGEN AND MAGNETITE FROM ROCK
Systems and methods for sequestering carbon, evolving hydrogen gas, producing iron oxide as magnetite, and producing magnesium carbonate as magnesite through sequential carbonation and serpentinization/hydration reactions involving processed olivine- and/or pyroxene-rich ores, as typically found in mafic and ultramafic igneous rock. Precious or scarce metals, such nickel, cobalt, chromium, rare earth elements, and others, may be concentrated in the remaining ore to facilitate their recovery from any gangue material.
HYDROGEN PRODUCTION AND SULFUR-CARBON SEQUESTRATION
Embodiments of the invention relate to producing hydrogen from a subsurface formation by injecting a reactant into the subsurface formation and reacting the reactant with the subsurface formation to form at least one of hydrogen gas or a mineralized product within the subsurface formation. The hydrogen produced is collected or one or more components of the reactant is sequestered to form a mineralized product in the subsurface formation. Other embodiments of the invention relate to producing hydrogen by injecting a thermal fluid into the subsurface rock formation, where the thermal fluid includes a reactant. The reactant is reacted with components in the subsurface formation to form at least one of hydrogen gas, mineralized sulfur, or mineralized carbon.
Composition for Generating Hydrogen
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 METHOD FOR THE PRODUCTION OF HYDROGEN
The present invention relates to a process of producing hydrogen gas from water, an iron-containing coal combustion product and carbon dioxide or a carbon dioxide precursor. The process is a spontaneous process that does not involve the implementation of external heating or electricity. The process further provides the recycling of the coal combustion product such as an iron slag or ash and may also be used for carbon dioxide sequestering.
PROCESS FOR PRODUCING A HYDROGEN-RICH GAS STREAM FROM ALUMINIUM WASTE
A process for the obtention of a hydrogen-rich gas stream from aluminium waste by obtaining a process water resulting from contacting aluminium salt slag with tap water, adding the process water of the previous step to an aluminium waste in a solution, and the hydrolysis of that solution to obtain the gas stream. The process is capable to obtain a yield of reaction close to 100% in higher reaction times.
METHOD OF OXIDATION IN A MOLTEN SALT BATH
A method for reusing waste including organic components in a bath of molten salt including providing to a reactor, at least one salt or a mixture of salts including at least one alkali metal hydroxide, providing the waste to the reactor, heating the at least one salt or mixture of salts in the reactor at a temperature above the melting point of the salt. Thus, the provided salt melts to form a liquid reaction medium, and induces an at least partial oxidation of the organic components. At least one compound resulting from this oxidation is recovered. At least one alkali metal hydroxide includes water of crystallisation, acting as oxidising agent for the organic compounds in the reaction medium, in such a way as to participate in the production of dihydrogen, the latter being recovered for the reuse thereof.
SYSTEM TO CONVERT COKE IN FLUID CATALYTIC CRACKING PROCESS BY UTILIZING METAL OXIDES WITH IN-SITU CO2 CAPTURE
This disclosure relates to systems and processes for reducing CO.sub.2 emissions produced by the regenerator reactor of the fluid catalytic cracking process.
Method For Directly Reducing A Material By Means Of Microwave Radiation
The present invention relates to the reduction of materials at low temperatures (<600° C.) by means of microwave radiation without needing to use chemical reducing agents or electrical contacts. It relates more specifically to a method for reducing a material, which comprises the following steps: applying microwave radiation to a material disposed in a microwave application cavity; and separating simultaneously the fluid oxidation products generated from the reduced material,
such that the method is carried out without chemical reducing agents or electrical contacts.
Microenvironment hydrogen-supplying breathable layer and applications thereof
A hydrogen-supplying breathable layer in the present disclosure comprises: a thin layer wrapping a hydrogen-producing formula inside, having an airtight outer side as well as an air-permeable inner side on which a plurality of micro pores are opened and featuring a monolayer or a composite layer; a hydrogen-producing formula wrapped inside the thin layer and not dissipated but absorbing moistures in air or liquid water for generation of hydrogen; hydrogen permeating a plurality of micro pores and released to skin and intra-corporal parts. The hydrogen-producing formula in the hydrogen-supplying breathable layer comprises metal peroxides (metal hydroxides or metal hydrides) and aluminum powders (or silica powders); the breathable layer is applicable to a dressing pack or other sanitary paraphernalia in daily lives for relieving non-bacteria inflammations and promoting health care effects.
Method of chemical looping reforming at low temperatures with hydrogen from water splitting
Chemical looping reform methods comprising heating an oxygen carrier in the presence of a catalyst and plasma radicals to react the oxygen carrier with a fuel to provide a reduced oxygen carrier; and contacting the reduced oxygen carrier with water or carbon dioxide to produce hydrogen or carbon monoxide, respectively, and regenerate the oxygen carrier. The chemical looping reform methods are carried out at low temperatures such as from 150° C. to 1000° C., preferably from 150° C. to 500° C. Catalyst used in the chemical looping reform methods include a sintered rare earth metal oxide oxygen carrier and perovskite. Methods of preparing the catalyst are also provided.