Disclosed is an absorbent containing an amine for absorption of an acid gas in a biogas, and a biogas purification system using the same.

Compositions are provided comprising pyrolysis carbon and humus containing materials to prevent wasteful water loss in turf grass applications by reducing evaporation, decreasing root zone and surface runoff, storing the water in the soil between irrigation events, and by increasing plant rooting depth enabling access to deeply held water in the soil; and methods for making and using the same.

A method of producing a fertiliser composition, the method comprising: •(a) providing partially decomposed organic matter; •(b) contacting the organic matter with: •(i) an anaerobic digestate; •(ii) a source of nitrate ion; •(iii) a source of ammonia; and •(c) contacting the mixture obtained in step (b) with a source of carbon dioxide. •Also claimed is a fertiliser composition comprising partially decomposed organic matter admixed with an anaerobic digestate, a source of nitrate ion, a source of ammonia and carbon dioxide.

Disclosed is a method for reducing methane emission from slurry (2) produced in a livestock farm (1). The method comprises the steps of guiding the slurry (2) from the livestock farm (1) to a dewatering unit (12) in which the slurry (2) is at least partially dewatered by extracting a watery fraction of said slurry (13), guiding the slurry from the dewatering unit (12) to a steam dryer (3), drying the slurry in the steam dryer (3), guiding the dried slurry (4) into a pyrolysis reactor (5) to produce pyrolysis gas (6) and biochar (7) through a pyrolysis process in the pyrolysis reactor (5), guiding at least a portion of the pyrolysis gas (6) to a combustion unit (8) in which the pyrolysis gas portion is combusted to raise the temperature of the combusted pyrolysis gas (9), guiding the combusted pyrolysis gas (9) to the pyrolysis reactor (5) to drive the pyrolysis process, guiding the combusted pyrolysis gas (9) from the pyrolysis reactor (5) to the steam dryer (3) to increase the temperature of steam (10) in the steam dryer (3), and heating the watery fraction of the slurry 13 to a temperature at least above 75° Celsius by means of the steam (10) from said steam dryer (3). Furthermore, a slurry treatment plant (20) for reducing methane emission from slurry (2) is disclosed.

According to present disclosure, there is disclosed an algae growth and cultivation system that provides a cost-efficient means of producing algae biomass as feedstock for algae-based products, such as, fertilizer, feed, biofuel manufacture, and desirably impacts, nutrient recovery from waste streams for valued byproducts production, recycle water, and alternative/renewable energy production. The system as discussed herein is an integrated systems approach to wastewater treatment, algal strains selection for byproducts production, and recycle of algal biomass-processing waste or additional algae harvested as feedstock for products such as fertilizer production. Embodiments of a system as discussed herein present an economically viable algae production system and process that allows algae-derived products such as fertilizer, feed, biofuels, etc. to compete with non-organic or petroleum products in the marketplace.

A mobile, self-contained system for enhancing plant growth comprising: a mobile structure comprising a plurality of wheels so that the system can be moved; a vessel supported by the structure; a recirculating pump supported by the structure and exterior to the vessel, the pump having a first discharge line and a second discharge line; a generator supported by the structure; a vessel outlet from a bottom portion of the vessel to the pump; and an aerator for injecting air into the first discharge line; wherein the first discharge line extends from the pump directly into the bottom portion of the vessel, such that the contents of the vessel can be recirculated by the pump from the vessel outlet back into the vessel through the first discharge line and the second discharge line extends from the pump and is adapted for discharging contents of the vessel directly into an irrigation system.

A fuel production system 1 includes a gasification unit 3; an electrolysis unit 60 that is connected to a renewable power generating unit 5 and a commercial power grid 8 and produces hydrogen using electric power; and a control unit 7 that determines a power index that depending on the carbon dioxide emission intensity of the electric power supplied from the commercial power grid 8. When the remaining amount of hydrogen is smaller than a lower threshold, the control unit 7 causes electric power to be supplied to the electrolysis unit 60 from the renewable power generating unit 5 and the commercial power grid 8 for production of hydrogen, and controls, based on the power index, the amount of hydrogen supplied by a hydrogen supply pump 64 and the amount of commercial power supply from the commercial power grid 8 to the electrolysis unit 60.

Methods for producing a solid ammonium bicarbonate product that includes preparing an organic feedstock that contains at least one nitrogen compound by causing organic animal manure and/or organic food waste to undergo anaerobic digestion, removing solids from the organic feedstock to produce an organic liquid effluent that contains at least one of ammonium and ammonia, performing a distillation process on the organic liquid effluent to strip and concentrate a vapor mixture therefrom that contains ammonia, carbon dioxide, and water and cool the vapor mixture to produce a condensed solution containing ammonium bicarbonate and/or ammonium carbonate, contacting the condensed solution with carbon dioxide to cause an ammonium bicarbonate precipitate to form from the condensed solution, and performing an evaporation process on the ammonium bicarbonate precipitate to remove water therefrom and produce the dry, solid ammonium bicarbonate product.

The invention is directed to organic fertilizers having commercial levels of nitrogen reacted with organic substances. The scalable process comprises adding an organic processing center to a fertilizer granulation plant specifically for the treatment of organics with an acid that acidifies, heats and liquifies a mix resulting in the hydrolysis of most or all organic material and polymers. For ammonium sulfate-based fertilizer this mix is only reacted with concentrated sulfuric acid. For ammonium phosphate fertilizers, this mix is reacted with both concentrated sulfuric acid and a concentrated phosphoric acid. The acidified organic mixes are piped to an existing or new granulation plant where it is injected with anhydrous ammonia in a tee mixer/reactor that results in a partially neutralized melt. Subsequently a sterilized and liquefied organic melt is sprayed over recycled bed material for production of granules before drying. Fertilizers made as disclosed provide a “green”, dual nitrogen-release profile when applied to crops releasing a bolus of nitrogen over one to two weeks following application followed by a slow or enhanced efficiency release of nitrogen over weeks of the growing season.

A process for the preparation of a soil inoculating composition comprising the steps of a) loading a vermicompost into a tank, b) adding a sufficient amount of water and molasses to vermicompost, c) breeding of microorganism in the mixture obtained in the step b), by adjusting the temperature to a range between 25-27° C. and by providing air into the mixture, d) forcing microorganism in the mixture obtained in the step c), to dormant state by d) adding a sufficient amount of molasses, e) bottling the composition obtained in the step d), for storage, f) resuscitating of microorganism in the stored composition from the dormant state to active state by diluting the composition with a sufficient amount of water before soil inoculation. An apparatus for producing soil inoculating composition comprising two concentric tanks wherein the inner tanks (104) holds the composition and the outer tank (101) acting as an heating system holds a liquid kept at a desired temperature by an heat control system (106).