A method and system for converting an aqueous salt containing sludge into gases and a solid residue is described. The sludge is pyrolyzed and gasified with the assistance of microwave radiation.

The fulvic acid solution production method of the present invention comprises: an apparatus preparation step of preparing a processing apparatus which comprises: a hermetic container internally having a closeable processing space; a steam jetting device operable to jet high-temperature and high-pressure steam into the hermetic container; a supply section having an opening-closing mechanism and operable to supply a raw material into the hermetic container; and a discharge section having an opening-closing mechanism and operable to discharge, to the outside, a processed liquid produced through processing of the raw material by the steam; a raw material input step of inputting a raw material containing chips of wood as a primary raw material, from the supply section into the processing space of the hermetic container of the processing apparatus; a stream introduction step of introducing steam having a temperature of 120 to 250° C. and a pressure of 12 to 35 atm into the processing space in which the raw material is input; a processing step of subjecting the raw material to a subcritical water reaction processing, under stirring, while introducing the steam; a mixed solution obtaining step of cooling the processed raw material after the processing step to obtain a mixed solution containing fulvic acid and humic acid; and a fulvic acid solution taking-out step of separating humic acid and fulvic acid from the obtained mixed solution to take out a fulvic acid solution.

Disclosed herein are processes, systems, and catalysts for improving pyrolysis technology. The disclosed processes and systems utilize a catalyst to increase pyrolysis gas (py-gas) and decrease bio-oil yields in pyrolysis reactions. The disclosed catalysts may include biochar derived from pyrolysis of industrial residuals, such as pyrolysis of wastewater biosolids (WB) and paper mill sludge (PMS). The disclosed catalysts also may include ash derived from incineration of wastewater biosolids (“biosolids incineration ash” (BIA)).

Disclosed herein are processes, systems, and catalysts for improving pyrolysis technology. The disclosed processes and systems utilize a catalyst to increase pyrolysis gas (py-gas) and decrease bio-oil yields in pyrolysis reactions. The disclosed catalysts may include biochar derived from pyrolysis of industrial residuals, such as pyrolysis of wastewater biosolids (WB) and paper mill sludge (PMS). The disclosed catalysts also may include ash derived from incineration of wastewater biosolids (“biosolids incineration ash” (BIA)).

The disclosure provides for the integration of a gas fermentation process with a gasification process whereby tail gas from the gas fermentation process is recycled to a dryer of the gasification process. The tail gas from the gas fermentation process is utilized to generate heat which in turn is used to dry feedstock to the gasification process. The heat is typically used to heat a drying gas, such as air, which is then directly or indirectly contacted with the gasification feedstock to dry the gasification feedstock. Dried gasification feedstock provides improved yield and improved quality of syngas as compared to gasification feedstock that is not dried.

The present invention relates to a new and novel process that combines treatment methods that use magnetite, Hydrothermal Carbonization (HTC), Hydrodynamic Cavitation (HDC), probiotics, and adsorption using Magnetic Hydrochar (MHC) and Water Treatment Residuals (WTR) to replace Activated Sludge Technology (AST) for the treatment of wastewater containing dissolved organic and inorganic contaminants.

The present invention discloses intelligent oil sludge treatment apparatuses and treatment processes. The treatment apparatus includes an integrative machine, an oil removal machine, a separation machine, a sludge collection tank, a dewatering machine, a pyrolysis machine, an agent tank, a deodorization tower, a crude oil tank, a light oil tank, a separator, a condenser, a desulfurization tower, a clean water tank, a sewage plant, and a steam boiler, where an outlet of the integrative machine is connected to an inlet of the oil removal machine; the oil removal machine is configured to remove crude oil from oil slurry; the oil removal machine collects the crude oil to the crude oil tank, discharges stench into the deodorization tower, and discharges the slurry into the separation machine; the separation machine is configured to perform a solid-liquid separation operation; the dewatering machine is configured to evaporate water and then convey same into the condenser, and to convey dry sludge into the pyrolysis machine; the pyrolysis machine is configured to convey pyrolysis gas into the condenser; the condenser is configured to discharge a condensate into the separator; an outlet of the separator is connected to the sewage plant and the light oil tank, separately; an inlet of the desulfurization tower is connected to the condenser, and an outlet thereof is connected to the steam boiler; the clean water tank is configured to supply a water source; and the steam boiler provides a heat source for the integrative machine and the oil removal machine.

An atmospheric pressure water ion generating device is arranged in a triphase organic matter pyrolysis system which includes a steam generating device and a pyrolysis and carbonization reaction device. The water ion generating device includes a connecting pipe connected with the steam generating device, and having an interior that is penetrated, a heating tube having a first end connected with the connecting pipe and having an interior provided with an air channel, and a spraying head connected with a second end of the heating tube, and having an interior that is tapered. The air channel has a surface provided with an alloy catalyst layer. The spraying head is provided with a nozzle which is connected with the pyrolysis and carbonization reaction device.

Described are methods and devices for the treatment of fecal matter. A column reactor is used to smolder fecal matter to produce and a volatile components stream and smoldered media. The volatile components stream may be subject to catalysis to reduce the emission of noxious substances and/or generate heat energy. Also described is the use of a turntable for removing smoldered media from the column reactor.

Described are methods and devices for the treatment of fecal matter. A column reactor is used to smolder fecal matter to produce and a volatile components stream and smoldered media. The volatile components stream may be subject to catalysis to reduce the emission of noxious substances and/or generate heat energy. Also described is the use of a turntable for removing smoldered media from the column reactor.