The invention relates to a system for generating superheated steam using hydrogen peroxide, formed by: a container for storing hydrogen peroxide, which stores a solution of peroxide that is used during the reaction to generate superheated steam; a hydrogen peroxide discharge pump connected to a first connecting duct, said discharge pump being used to pump the hydrogen peroxide solution to a reaction container via a second connecting duct; and a steam generating reaction container or reactor, in which the reaction takes place and the superheated steam is generated, said reaction container or reactor receiving the hydrogen peroxide solution in order for the reaction to take place and the superheated steam to be generated and subsequently conveyed through a nozzle and an outlet duct towards installations that are to undergo cleaning and/or stimulation.

A method is disclosed for nitrogen recovery from an ammonium including fluid and a bio-electrochemical system for the same. In an embodiment, the method includes providing an anode compartment including an anode; providing a cathode compartment including a cathode, wherein the compartments are separated by at least one ion exchange membrane; providing the ammonium comprising fluid in the anode compartment and a second fluid in the cathode compartment; applying a voltage between the anode and the cathode; and extracting nitrogen from the cathode compartment.

A method is disclosed for nitrogen recovery from an ammonium including fluid and a bio-electrochemical system for the same. In an embodiment, the method includes providing an anode compartment including an anode; providing a cathode compartment including a cathode, wherein the compartments are separated by at least one ion exchange membrane; providing the ammonium comprising fluid in the anode compartment and a second fluid in the cathode compartment; applying a voltage between the anode and the cathode; and extracting nitrogen from the cathode compartment.

A method for producing a purified, stable, dioxytetrahydride compressible gas from water. The gas is suitable for a variety of uses and may also be infused into water which itself is useful for a variety of purposes.

A process for producing black powder oxygen carriers for use in a chemical looping combustion unit includes the steps of: (a) removing and collecting the black powder waste material that was formed in a gas pipeline; (b) pre-treating the collected black powder to adjust its spherical shape to avoid attrition and fines production; and (c) activating the black powder to increase its reactivity rate and produce the black powder oxygen carrier that is suitable for use in the chemical looping combustion process as an oxygen carrier.

A process for producing black powder oxygen carriers for use in a chemical looping combustion unit includes the steps of: (a) removing and collecting the black powder waste material that was formed in a gas pipeline; (b) pre-treating the collected black powder to adjust its spherical shape to avoid attrition and fines production; and (c) activating the black powder to increase its reactivity rate and produce the black powder oxygen carrier that is suitable for use in the chemical looping combustion process as an oxygen carrier.

A method for producing deuterium-depleted water by removing heavy water and semi-heavy water from water includes an adsorption step of supplying water vapor to a predetermined adsorbent at pressure at which heavy water and semi-heavy water are adsorbed by the adsorbent and light water is not easily adsorbed, causing the heavy water and semi-heavy water to be adsorbed, and recovering the water vapor not adsorbed by the adsorbent. The method also includes a desorption step of maintaining vapor pressure around the predetermined adsorbent which has adsorbed the water vapor in a range in which light water is desorbed and heavy water or semi-heavy water is not easily desorbed, and recovering the water vapor desorbed from the adsorbent.

A method for producing deuterium-depleted water by removing heavy water and semi-heavy water from water includes an adsorption step of supplying water vapor to a predetermined adsorbent at pressure at which heavy water and semi-heavy water are adsorbed by the adsorbent and light water is not easily adsorbed, causing the heavy water and semi-heavy water to be adsorbed, and recovering the water vapor not adsorbed by the adsorbent. The method also includes a desorption step of maintaining vapor pressure around the predetermined adsorbent which has adsorbed the water vapor in a range in which light water is desorbed and heavy water or semi-heavy water is not easily desorbed, and recovering the water vapor desorbed from the adsorbent.

A method for biological hydrosynthesis, energy generation and storage and/or topsoil restoration comprising the steps of: undertaking a primary amendment of a site with a first catalyst and a second catalyst, wherein the first catalyst and the second catalyst are applied to at least a portion of the site such that a matrix of biological energy generation points are constructed on about 5% of the site by area; undertaking a secondary amendment of the site with the first catalyst and the second catalyst, wherein the first catalyst and the second catalyst are applied to at least a portion of the site such that a matrix of biological energy generation points are constructed on about 20% of the site by area, and undertaking a tertiary amendment of the site with the first catalyst and the second catalyst, wherein the first catalyst and the second catalyst are applied to at least a portion of the site such that a matrix of biological energy generation points are constructed on about 75% of the site by area, wherein the primary amendment, the secondary amendment and the tertiary amendment of the site are each conducted at least once.

A method for biological hydrosynthesis, energy generation and storage and/or topsoil restoration comprising the steps of: undertaking a primary amendment of a site with a first catalyst and a second catalyst, wherein the first catalyst and the second catalyst are applied to at least a portion of the site such that a matrix of biological energy generation points are constructed on about 5% of the site by area; undertaking a secondary amendment of the site with the first catalyst and the second catalyst, wherein the first catalyst and the second catalyst are applied to at least a portion of the site such that a matrix of biological energy generation points are constructed on about 20% of the site by area, and undertaking a tertiary amendment of the site with the first catalyst and the second catalyst, wherein the first catalyst and the second catalyst are applied to at least a portion of the site such that a matrix of biological energy generation points are constructed on about 75% of the site by area, wherein the primary amendment, the secondary amendment and the tertiary amendment of the site are each conducted at least once.